Chemical Properties of 1-Decene (CAS 872-05-9)

InChI

InChI=1S/C10H20/c1-3-5-7-9-10-8-6-4-2/h3H,1,4-10H2,2H3

InChI Key

AFFLGGQVNFXPEV-UHFFFAOYSA-N

Formula

C10H20

SMILES

C=CCCCCCCCC

Molecular Weight¹

140.27

CAS

872-05-9

Other Names

• 1-C10H20
• 1-n-Decene
• Decene-1
• Decylene
• Gulftene 10
• Linealene 10
• NSC 62122
• Neodene 10
• dec-1-ene
• n-1-Decene
• «alpha»-Decene

• ω : Acentric Factor.
• T_ig : Autoignition Temperature (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).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire 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.

Physical Properties

Property	Value	Unit	Source
ω	[0.4805; 0.4912]
ω	0.4910		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.4912		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.4805		ChemSep v8.3 pure component data Compiled value
ω	0.4910		KDB
Tig	508.15	K	KDB
ΔcH°liquid	-6619.60 ± 1.80	kJ/mol	NIST
μ	0.42	debye	ChemSep v8.3 pure component data Compiled value
Tflash,cc	326.48	K	KDB
ΔfG°	[121.10; 122.70]	kJ/mol
ΔfG°	122.70	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	121.10	kJ/mol	KDB
ΔfH°gas	[-124.60; -122.10]	kJ/mol
ΔfH°gas	-122.10	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-124.20	kJ/mol	KDB
ΔfH°gas	-124.60	kJ/mol	NIST
ΔfH°gas	-123.40	kJ/mol	NIST
ΔfH°liquid	-173.80 ± 1.90	kJ/mol	NIST
ΔfusH°	20.38	kJ/mol	Joback Calculated Property
ΔvapH°	[50.40; 50.50]	kJ/mol
ΔvapH°	50.44	kJ/mol	NIST
ΔvapH°	50.43 ± 0.20	kJ/mol	NIST
ΔvapH°	50.40 ± 0.20	kJ/mol	NIST
ΔvapH°	50.50	kJ/mol	NIST
IE	[9.42; 9.59]	eV
IE	9.42 ± 0.01	eV	NIST
IE	9.48	eV	NIST
IE	9.42 ± 0.01	eV	NIST
IE	9.59 ± 0.01	eV	NIST
log10WS	[-5.51; -5.51]
log10WS	-5.51		Aq. Solubility Prediction
log10WS	-5.51		Estimated Solubility
logPoct/wat	3.923		Crippen Calculated Property
McVol	147.460	ml/mol	McGowan Calculated Property
NFPA Fire	2		KDB
Pc	[2206.32; 2223.00]	kPa
Pc	2220.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Pc	2208.89	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	2206.32	kPa	Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc	2223.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	2220.00	kPa	KDB
Pc	2220.00 ± 100.00	kPa	NIST
Ptriple	2.59e-05	kPa	ChemSep v8.3 pure component data Compiled value
ρc	238.45 ± 14.03	kg/m3	NIST
Inp	[153.90; 997.00]
Inp	985.00		NIST
Inp	982.00		NIST
Inp	989.00		NIST
Inp	990.00		NIST
Inp	985.10		NIST
Inp	985.00		NIST
Inp	988.00		NIST
Inp	989.00		NIST
Inp	989.00		NIST
Inp	989.00		NIST
Inp	988.60		NIST
Inp	990.00		NIST
Inp	989.00		NIST
Inp	988.00		NIST
Inp	989.00		NIST
Inp	982.00		NIST
Inp	983.00		NIST
Inp	982.00		NIST
Inp	990.00		NIST
Inp	989.20		NIST
Inp	990.10		NIST
Inp	982.70		NIST
Inp	982.20		NIST
Inp	987.00		NIST
Inp	988.00		NIST
Inp	990.00		NIST
Inp	992.00		NIST
Inp	988.00		NIST
Inp	988.00		NIST
Inp	992.50		NIST
Inp	993.00		NIST
Inp	992.00		NIST
Inp	987.00		NIST
Inp	993.00		NIST
Inp	993.00		NIST
Inp	989.20		NIST
Inp	989.50		NIST
Inp	990.70		NIST
Inp	985.00		NIST
Inp	989.20		NIST
Inp	989.50		NIST
Inp	990.70		NIST
Inp	988.00		NIST
Inp	988.74		NIST
Inp	988.81		NIST
Inp	988.83		NIST
Inp	991.63		NIST
Inp	991.76		NIST
Inp	991.73		NIST
Inp	988.00		NIST
Inp	991.00		NIST
Inp	982.00		NIST
Inp	997.00		NIST
Inp	989.00		NIST
Inp	989.00		NIST
Inp	989.00		NIST
Inp	991.00		NIST
Inp	991.00		NIST
Inp	992.00		NIST
Inp	992.00		NIST
Inp	989.00		NIST
Inp	989.00		NIST
Inp	988.00		NIST
Inp	988.80		NIST
Inp	988.00		NIST
Inp	988.00		NIST
Inp	997.00		NIST
Inp	988.00		NIST
Inp	988.00		NIST
Inp	987.00		NIST
Inp	986.00		NIST
Inp	990.00		NIST
Inp	991.00		NIST
Inp	982.00		NIST
Inp	988.00		NIST
Inp	Outlier 157.60		NIST
Inp	Outlier 153.90		NIST
Inp	Outlier 157.60		NIST
Inp	Outlier 153.90		NIST
Inp	993.00		NIST
Inp	989.20		NIST
Inp	989.50		NIST
Inp	988.83		NIST
Ip	[1020.00; 1061.00]
Ip	1052.00		NIST
Ip	1054.00		NIST
Ip	1055.00		NIST
Ip	1048.00		NIST
Ip	1050.00		NIST
Ip	1046.00		NIST
Ip	1047.00		NIST
Ip	1046.00		NIST
Ip	1051.70		NIST
Ip	1055.30		NIST
Ip	1048.50		NIST
Ip	1049.80		NIST
Ip	1051.70		NIST
Ip	1055.30		NIST
Ip	1048.50		NIST
Ip	1049.80		NIST
Ip	1047.00		NIST
Ip	1061.00		NIST
Ip	Outlier 1020.00		NIST
Ip	1054.00		NIST
Ip	1043.00		NIST
Ip	1035.00		NIST
Ip	1039.00		NIST
Ip	1047.00		NIST
Ip	1043.00		NIST
S°liquid	425.01	J/mol×K	NIST
Tboil	[427.00; 446.30]	K
Tboil	443.75	K	ChemSep v8.3 pure component data Compiled value
Tboil	443.60	K	KDB
Tboil	443.70	K	NIST
Tboil	444.90 ± 1.00	K	NIST
Tboil	444.90 ± 0.50	K	NIST
Tboil	Outlier 429.00 ± 6.00	K	NIST
Tboil	442.00 ± 3.00	K	NIST
Tboil	443.75 ± 0.25	K	NIST
Tboil	443.70 ± 2.00	K	NIST
Tboil	446.30 ± 1.50	K	NIST
Tboil	443.80 ± 1.50	K	NIST
Tboil	433.60 ± 6.00	K	NIST
Tboil	444.00 ± 6.00	K	NIST
Tboil	435.00 ± 6.00	K	NIST
Tboil	445.00 ± 4.00	K	NIST
Tboil	Outlier 427.00 ± 3.00	K	NIST
Tc	[614.82; 617.00]	K
Tc	617.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Tc	615.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	614.82	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	616.60	K	ChemSep v8.3 pure component data Compiled value
Tc	617.00	K	KDB
Tc	617.00 ± 2.00	K	NIST
Tfus	[206.51; 209.15]	K
Tfus	207.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	206.90	K	ChemSep v8.3 pure component data Compiled value
Tfus	206.90	K	KDB
Tfus	207.06	K	Aq. Solubility Prediction
Tfus	Outlier 209.15 ± 1.00	K	NIST
Tfus	206.51 ± 0.15	K	NIST
Tfus	206.82 ± 0.05	K	NIST
Tfus	206.84 ± 0.03	K	NIST
Tfus	206.90 ± 0.50	K	NIST
Tfus	206.90 ± 0.60	K	NIST
Ttriple	[206.47; 206.90]	K
Ttriple	206.90	K	ChemSep v8.3 pure component data Compiled value
Ttriple	206.89 ± 0.05	K	NIST
Ttriple	206.89 ± 0.06	K	NIST
Ttriple	206.88 ± 0.06	K	NIST
Ttriple	Outlier 206.47 ± 0.20	K	NIST
Ttriple	206.89 ± 0.05	K	NIST
UQi	5.80		ChemSep v8.3 pure component data Compiled value
URi	6.97		ChemSep v8.3 pure component data Compiled value
Vc	[0.584; 0.584]	m3/kmol
Vc	0.584	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Vc	0.584	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.584	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.584	m3/kmol	KDB
Vc	0.584	m3/kmol	NIST
VCOSTALD	0.60	m3/kmol	Hankinson and Thomson (1979), COSTALD parameters Compiled value
ωSRK	0.50		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zc	[0.2527230; 0.2530000]
Zc	0.2530000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Zc	0.2530000		ChemSep v8.3 pure component data Compiled value
Zc	0.2527230		KDB
Zra	[0.25; 0.25]
Zra	0.25		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zra	0.25		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	300.83	J/mol×K	298.15	NIST
Csat	[275.60; 330.70]	J/mol×K	[210.00; 360.00]
Csat	275.70	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	275.60	J/mol×K	220.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	276.60	J/mol×K	230.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	278.30	J/mol×K	240.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	280.80	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	284.00	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	287.70	J/mol×K	270.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	289.00	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	291.90	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	296.40	J/mol×K	290.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	300.30	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	301.20	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	306.20	J/mol×K	310.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	311.30	J/mol×K	320.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	316.40	J/mol×K	330.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	321.40	J/mol×K	340.00	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	326.20	J/mol×K	350.00	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	330.70	J/mol×K	360.00	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	[7.95; 13.81]	kJ/mol	[198.30; 206.90]
ΔfusH	7.95	kJ/mol	198.30	NIST
ΔfusH	13.81	kJ/mol	206.90	NIST
ΔfusH	13.81	kJ/mol	206.90	NIST
ΔvapH	[38.66; 45.10]	kJ/mol	[402.50; 443.70]
ΔvapH	45.10	kJ/mol	402.50	NIST
ΔvapH	43.80	kJ/mol	414.00	NIST
ΔvapH	38.66	kJ/mol	443.70	KDB
n0	[1.42139; 1.42140]		[293.15; 293.15]
n0	1.42139		293.15	Excess Volume of the 1-Propanol + 1-Alkene Systems in Terms of an Equation of State with Association
n0	1.42140		293.15	Isobaric Vapor-Liquid Equilibria of Hexane + 1-Decene and Octane + 1-Decene Mixtures
ρl	741.00	kg/m3	293.00	KDB
ΔfusS	[40.09; 66.73]	J/mol×K	[198.30; 206.90]
ΔfusS	40.09	J/mol×K	198.30	NIST
ΔfusS	66.73	J/mol×K	206.90	NIST
γ	0.02	N/m	298.20	KDB

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[171.53; 582.20]	J/mol×K	[206.90; 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			1.33732e+02
Coefficient B			-5.92840e+02
Coefficient C			6.48979e+00
Coefficient D			4.30271e-05
Coefficient E			-2.36742e-08
Temperature range, min.			206.90
Temperature range, max.			1500.00
Cp,gas	171.53	J/mol×K	206.90	Calculated Property
Cp,gas	256.58	J/mol×K	350.58	Calculated Property
Cp,gas	335.24	J/mol×K	494.26	Calculated Property
Cp,gas	398.35	J/mol×K	637.93	Calculated Property
Cp,gas	448.07	J/mol×K	781.61	Calculated Property
Cp,gas	487.50	J/mol×K	925.29	Calculated Property
Cp,gas	519.08	J/mol×K	1068.97	Calculated Property
Cp,gas	544.60	J/mol×K	1212.64	Calculated Property
Cp,gas	565.34	J/mol×K	1356.32	Calculated Property
Cp,gas	582.20	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[275.41; 411.25]	J/mol×K	[206.89; 494.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,liquid in J/mol×K, T in K
Coefficient A			4.17440e+02
Coefficient B			-1.61650e+00
Coefficient C			5.39480e-03
Coefficient D			-4.34800e-06
Coefficient E			0.00000e+00
Temperature range, min.			206.89
Temperature range, max.			494.00
Cp,liquid	275.41	J/mol×K	206.89	Calculated Property
Cp,liquid	279.85	J/mol×K	238.79	Calculated Property
Cp,liquid	288.92	J/mol×K	270.69	Calculated Property
Cp,liquid	301.79	J/mol×K	302.59	Calculated Property
Cp,liquid	317.61	J/mol×K	334.49	Calculated Property
Cp,liquid	335.53	J/mol×K	366.40	Calculated Property
Cp,liquid	354.69	J/mol×K	398.30	Calculated Property
Cp,liquid	374.27	J/mol×K	430.20	Calculated Property
Cp,liquid	393.40	J/mol×K	462.10	Calculated Property
Cp,liquid	411.25	J/mol×K	494.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0049754; 0.0002064]	Pa×s	[206.89; 443.75]	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			-1.58680e+01
Coefficient B			1.43480e+03
Coefficient C			6.80710e-01
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			206.89
Temperature range, max.			443.75
η	0.0049754	Pa×s	206.89	Calculated Property
η	0.0024680	Pa×s	233.21	Calculated Property
η	0.0014223	Pa×s	259.53	Calculated Property
η	0.0009130	Pa×s	285.84	Calculated Property
η	0.0006349	Pa×s	312.16	Calculated Property
η	0.0004693	Pa×s	338.48	Calculated Property
η	0.0003637	Pa×s	364.80	Calculated Property
η	0.0002927	Pa×s	391.11	Calculated Property
η	0.0002428	Pa×s	417.43	Calculated Property
η	0.0002064	Pa×s	443.75	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[53.52; 0.00]	kJ/mol	[206.89; 616.60]	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			6.69850e+01
Coefficient B			7.69440e-01
Coefficient C			-7.99750e-01
Coefficient D			4.23790e-01
Coefficient E			1.00000e-03
Critical temperature, Tc (K)			6.16600e+02
Temperature range, min.			206.89
Temperature range, max.			616.60
ΔvapH	53.52	kJ/mol	206.89	Calculated Property
ΔvapH	51.13	kJ/mol	252.41	Calculated Property
ΔvapH	48.73	kJ/mol	297.94	Calculated Property
ΔvapH	46.22	kJ/mol	343.46	Calculated Property
ΔvapH	43.47	kJ/mol	388.98	Calculated Property
ΔvapH	40.30	kJ/mol	434.51	Calculated Property
ΔvapH	36.43	kJ/mol	480.03	Calculated Property
ΔvapH	31.39	kJ/mol	525.55	Calculated Property
ΔvapH	24.05	kJ/mol	571.08	Calculated Property
ΔvapH	0.00	kJ/mol	616.60	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[326.18; 467.83]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.48286e+01
Coefficient B			-3.90202e+03
Coefficient C			-5.78340e+01
Temperature range, min.			326.18
Temperature range, max.			467.83
Pvap	1.33	kPa	326.18	Calculated Property
Pvap	2.98	kPa	341.92	Calculated Property
Pvap	6.14	kPa	357.66	Calculated Property
Pvap	11.74	kPa	373.40	Calculated Property
Pvap	21.13	kPa	389.14	Calculated Property
Pvap	36.05	kPa	404.87	Calculated Property
Pvap	58.72	kPa	420.61	Calculated Property
Pvap	91.83	kPa	436.35	Calculated Property
Pvap	138.58	kPa	452.09	Calculated Property
Pvap	202.63	kPa	467.83	Calculated Property
Pvap	[2.59e-05; 2223.43]	kPa	[206.89; 616.60]	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			6.14932e+01
Coefficient B			-7.77690e+03
Coefficient C			-6.46370e+00
Coefficient D			6.37500e-18
Coefficient E			6.00000e+00
Temperature range, min.			206.89
Temperature range, max.			616.60
Pvap	2.59e-05	kPa	206.89	Calculated Property
Pvap	6.30e-03	kPa	252.41	Calculated Property
Pvap	0.24	kPa	297.94	Calculated Property
Pvap	3.06	kPa	343.46	Calculated Property
Pvap	19.61	kPa	388.98	Calculated Property
Pvap	79.52	kPa	434.51	Calculated Property
Pvap	236.15	kPa	480.03	Calculated Property
Pvap	565.94	kPa	525.55	Calculated Property
Pvap	1173.71	kPa	571.08	Calculated Property
Pvap	2223.43	kPa	616.60	Calculated Property
Pvap	[1.46e-05; 2193.34]	kPa	[206.89; 617.05]	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			1.10936e+02
Coefficient B			-9.75380e+03
Coefficient C			-1.41204e+01
Coefficient D			8.63327e-06
Coefficient E			0.00000e+00
Temperature range, min.			206.89
Temperature range, max.			617.05
Pvap	1.46e-05	kPa	206.89	Calculated Property
Pvap	5.24e-03	kPa	252.46	Calculated Property
Pvap	0.23	kPa	298.04	Calculated Property
Pvap	3.04	kPa	343.61	Calculated Property
Pvap	19.43	kPa	389.18	Calculated Property
Pvap	77.82	kPa	434.76	Calculated Property
Pvap	229.39	kPa	480.33	Calculated Property
Pvap	550.65	kPa	525.90	Calculated Property
Pvap	1151.02	kPa	571.48	Calculated Property
Pvap	2193.34	kPa	617.05	Calculated Property
Pvap	[6.36; 104.15]	kPa	[359.92; 444.80]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.40118e+01
Coefficient B			-3.45819e+03
Coefficient C			-7.55720e+01
Reference			Forziati, Camin, et al., 1950, 2
Temperature range, min.			359.92
Temperature range, max.			444.80
Pvap	6.36	kPa	359.92	Calculated Property
Pvap	9.40	kPa	369.35	Calculated Property
Pvap	13.55	kPa	378.78	Calculated Property
Pvap	19.12	kPa	388.21	Calculated Property
Pvap	26.43	kPa	397.64	Calculated Property
Pvap	35.87	kPa	407.08	Calculated Property
Pvap	47.87	kPa	416.51	Calculated Property
Pvap	62.90	kPa	425.94	Calculated Property
Pvap	81.48	kPa	435.37	Calculated Property
Pvap	104.15	kPa	444.80	Calculated Property
Pvap	[6.36; 104.15]	kPa	[359.92; 444.80]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.40118e+01
Coefficient B			-3.45819e+03
Coefficient C			-7.55720e+01
Reference			Forziati, Camin, et al., 1950
Temperature range, min.			359.92
Temperature range, max.			444.80
Pvap	6.36	kPa	359.92	Calculated Property
Pvap	9.40	kPa	369.35	Calculated Property
Pvap	13.55	kPa	378.78	Calculated Property
Pvap	19.12	kPa	388.21	Calculated Property
Pvap	26.43	kPa	397.64	Calculated Property
Pvap	35.87	kPa	407.08	Calculated Property
Pvap	47.87	kPa	416.51	Calculated Property
Pvap	62.90	kPa	425.94	Calculated Property
Pvap	81.48	kPa	435.37	Calculated Property
Pvap	104.15	kPa	444.80	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[804.11; 240.40]	kg/m3	[206.89; 616.60]	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			6.16903e+01
Coefficient B			2.56610e-01
Coefficient C			6.16600e+02
Coefficient D			2.91480e-01
Temperature range, min.			206.89
Temperature range, max.			616.60
ρl	804.11	kg/m3	206.89	Calculated Property
ρl	772.00	kg/m3	252.41	Calculated Property
ρl	738.38	kg/m3	297.94	Calculated Property
ρl	702.86	kg/m3	343.46	Calculated Property
ρl	664.89	kg/m3	388.98	Calculated Property
ρl	623.63	kg/m3	434.51	Calculated Property
ρl	577.61	kg/m3	480.03	Calculated Property
ρl	523.84	kg/m3	525.55	Calculated Property
ρl	454.27	kg/m3	571.08	Calculated Property
ρl	240.40	kg/m3	616.60	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.01]	N/m	[207.15; 443.75]	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			5.09425e-02
Coefficient B			-9.19000e-05
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			207.15
Temperature range, max.			443.75
γ	0.03	N/m	207.15	Calculated Property
γ	0.03	N/m	233.44	Calculated Property
γ	0.03	N/m	259.73	Calculated Property
γ	0.02	N/m	286.02	Calculated Property
γ	0.02	N/m	312.31	Calculated Property
γ	0.02	N/m	338.59	Calculated Property
γ	0.02	N/m	364.88	Calculated Property
γ	0.01	N/m	391.17	Calculated Property
γ	0.01	N/m	417.46	Calculated Property
γ	0.01	N/m	443.75	Calculated Property
γ	[0.03; 0.00]	N/m	[206.89; 616.60]	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 γ in N/m, T in K
Coefficient A			5.43780e-02
Coefficient B			1.25930e+00
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			1.00000e-07
Critical temperature, Tc (K)			6.16600e+02
Temperature range, min.			206.89
Temperature range, max.			616.60
γ	0.03	N/m	206.89	Calculated Property
γ	0.03	N/m	252.41	Calculated Property
γ	0.02	N/m	297.94	Calculated Property
γ	0.02	N/m	343.46	Calculated Property
γ	0.02	N/m	388.98	Calculated Property
γ	0.01	N/m	434.51	Calculated Property
γ	0.01	N/m	480.03	Calculated Property
γ	0.00	N/m	525.55	Calculated Property
γ	0.00	N/m	571.08	Calculated Property
γ	0.00	N/m	616.60	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.02; 0.09]	W/m×K	[443.75; 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			2.72320e-05
Coefficient B			1.25700e+00
Coefficient C			7.51700e+02
Coefficient D			0.00000e+00
Temperature range, min.			443.75
Temperature range, max.			1000.00
λgas	0.02	W/m×K	443.75	Calculated Property
λgas	0.03	W/m×K	505.56	Calculated Property
λgas	0.03	W/m×K	567.36	Calculated Property
λgas	0.04	W/m×K	629.17	Calculated Property
λgas	0.05	W/m×K	690.97	Calculated Property
λgas	0.06	W/m×K	752.78	Calculated Property
λgas	0.06	W/m×K	814.58	Calculated Property
λgas	0.07	W/m×K	876.39	Calculated Property
λgas	0.08	W/m×K	938.19	Calculated Property
λgas	0.09	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.15; 0.10]	W/m×K	[206.89; 443.75]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is λliquid in W/m×K, T in K
Coefficient A			2.02370e-01
Coefficient B			-2.41870e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			206.89
Temperature range, max.			443.75
λliquid	0.15	W/m×K	206.89	Calculated Property
λliquid	0.15	W/m×K	233.21	Calculated Property
λliquid	0.14	W/m×K	259.53	Calculated Property
λliquid	0.13	W/m×K	285.84	Calculated Property
λliquid	0.13	W/m×K	312.16	Calculated Property
λliquid	0.12	W/m×K	338.48	Calculated Property
λliquid	0.11	W/m×K	364.80	Calculated Property
λliquid	0.11	W/m×K	391.11	Calculated Property
λliquid	0.10	W/m×K	417.43	Calculated Property
λliquid	0.10	W/m×K	443.75	Calculated Property

Similar Compounds

Find more compounds similar to 1-Decene.

Mixtures

• 1-Decene + 1-Hexanol
• n-Hexane + 1-Decene
• 1-Decene + Octane
• Propanamide, N,N-bis(2-ethylhexyl)-2-methyl- + 1-Decene
• 1-Decene + 1,8-Diaminooctane
• 1-Decene + 1,1O-DIAMINODECANE
• 1-Decene + 1,12-Dodecanediamine
• 1-Propanol + 1-Decene
• 1-Decene + Dimethyl ether

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.
• 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
• Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
• 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 of alkanes and alkenes in 1-alkyl-3-methylimidazolium tetrafluoroborate
• 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 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
• Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
• 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 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
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate [EMIM][TCB] using gas liquid chromatography
• Activity coefficients at infinite dilution of organic solutes in N-alkylpyridinium bis(trifluoromethylsulfonyl)imide ([CnPY][NTf2], n = 2, 4, 5) using gas liquid chromatography
• 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
• 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
• 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 and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
• Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
• The study of activity coefficients at infinite dilution for organic solutes and water in 1-butyl-4-methylpyridinium dicyanamide, [B4MPy][DCA] using GLC
• Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Activity coefficients at infinite dilution for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
• Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
• A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
• Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in 1-allyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}imide ionic liquid
• Separation of aliphatic from aromatic hydrocarbons and sulphur compounds from fuel based on measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid N,N-diethyl-N-methyl-N-(2-methoxy-ethyl)ammonium bis(trifluoromethylsulfonyl)imide
• Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
• 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
• Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
• Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
• 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
• Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
• 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
• Excess Volume of the 1-Propanol + 1-Alkene Systems in Terms of an Equation of State with Association
• Activity Coefficients at Infinite Dilution by GLC in Alkanediamines as Stationary Phases
• Biomass-Derived Platform Chemicals: Thermodynamic Studies on the Extraction of 5-Hydroxymethylfurfural from Ionic Liquids
• Isothermal Phase Equilibria and Excess Molar Enthalpies for Binary Systems with Dimethyl Ether at 323.15 K
• Isobaric Vapor-Liquid Equilibria of Hexane + 1-Decene and Octane + 1-Decene Mixtures
• Paramagnetic Ionic Liquid 1-Butyl-3-methylimidazolium Tetrabromidocobaltate(II): Activity Coefficients at Infinite Dilution of Organic Solutes and Crystal Structure
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tris(pentafluoroethyl)trifluorophosphate [EMIM][FAP] Using Gas-Liquid Chromatography
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure
• Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD

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