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).
• 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_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_c : Critical density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• 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).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.4910		KDB
Tig	508.15	K	KDB
ΔcH°liquid	-6619.60 ± 1.80	kJ/mol	NIST
Tflash,cc	326.48	K	KDB
ΔfG°	121.10	kJ/mol	KDB
ΔfH°gas	[-124.60; -123.40]	kJ/mol
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	[2220.00; 2220.00]	kPa
Pc	2220.00	kPa	KDB
Pc	2220.00 ± 100.00	kPa	NIST
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
I	[1020.00; 1061.00]
I	1052.00		NIST
I	1054.00		NIST
I	1055.00		NIST
I	1048.00		NIST
I	1050.00		NIST
I	1046.00		NIST
I	1047.00		NIST
I	1046.00		NIST
I	1051.70		NIST
I	1055.30		NIST
I	1048.50		NIST
I	1049.80		NIST
I	1051.70		NIST
I	1055.30		NIST
I	1048.50		NIST
I	1049.80		NIST
I	1047.00		NIST
I	1061.00		NIST
I	Outlier 1020.00		NIST
I	1054.00		NIST
I	1043.00		NIST
I	1035.00		NIST
I	1039.00		NIST
I	1047.00		NIST
I	1043.00		NIST
S°liquid	425.01	J/mol×K	NIST
Tboil	[427.00; 446.30]	K
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	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	[617.00; 617.00]	K
Tc	617.00	K	KDB
Tc	617.00 ± 2.00	K	NIST
Tfus	[206.51; 209.15]	K
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; 206.89]	K
Ttriple	206.89 ± 0.05	K	NIST
Ttriple	206.89 ± 0.06	K	NIST
Ttriple	206.88 ± 0.06	K	NIST
Ttriple	206.47 ± 0.20	K	NIST
Ttriple	206.89 ± 0.05	K	NIST
Vc	[0.584; 0.584]	m3/kmol
Vc	0.584	m3/kmol	KDB
Vc	0.584	m3/kmol	NIST
Zc	0.2527230		KDB
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	[207.81; 506.73]	J/mol×K	[273.00; 1000.00]	Joback Predicted correlation
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K
Coefficient A			-9.19300e+00
Coefficient B			9.33820e-01
Coefficient C			-5.43100e-04
Coefficient D			1.25200e-07
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	207.81	J/mol×K	273.00	Calculated Property
Cp,gas	258.74	J/mol×K	353.78	Calculated Property
Cp,gas	304.32	J/mol×K	434.56	Calculated Property
Cp,gas	344.94	J/mol×K	515.33	Calculated Property
Cp,gas	381.00	J/mol×K	596.11	Calculated Property
Cp,gas	412.89	J/mol×K	676.89	Calculated Property
Cp,gas	441.02	J/mol×K	757.67	Calculated Property
Cp,gas	465.76	J/mol×K	838.44	Calculated Property
Cp,gas	487.54	J/mol×K	919.22	Calculated Property
Cp,gas	506.73	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0044561; 0.0002241]	Pa×s	[206.85; 431.90]	Joback Predicted correlation
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-1.11514e+01
Coefficient B			1.18688e+03
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			206.85
Temperature range, max.			431.90
η	0.0044561	Pa×s	206.85	Calculated Property
η	0.0023999	Pa×s	231.85	Calculated Property
η	0.0014580	Pa×s	256.86	Calculated Property
η	0.0009677	Pa×s	281.86	Calculated Property
η	0.0006866	Pa×s	306.87	Calculated Property
η	0.0005130	Pa×s	331.88	Calculated Property
η	0.0003993	Pa×s	356.88	Calculated Property
η	0.0003212	Pa×s	381.89	Calculated Property
η	0.0002653	Pa×s	406.89	Calculated Property
η	0.0002241	Pa×s	431.90	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	[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

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
• 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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