Chemical Properties of 1-Hexadecanol (CAS 124-29-8)

InChI

InChI=1S/C16H34O/c1-2-3-4-5-6-7-8-9-10-11-12-13-14-15-16-17/h17H,2-16H2,1H3

InChI Key

BXWNKGSJHAJOGX-UHFFFAOYSA-N

Formula

C16H34O

SMILES

CCCCCCCCCCCCCCCCO

Molecular Weight¹

242.44

CAS

124-29-8

Other Names

• 1-Cetanol
• 1-Hexadecyl alcohol
• 1-Hexanedecanol
• 1-Hydroxyhexadecane
• 19141-82-3
• Adol 52
• Adol 52 NF
• Adol 520
• Adol 54
• Alcohol c-16
• Aldol 54
• Alfol 16
• Alfol 16RD
• Atalco C
• CO-1670
• CO-1695
• Cachalot C-50
• Cachalot C-50 NF
• Cachalot C-51
• Cachalot C-52
• Cetaffine
• Cetal
• Cetalol CA
• Cetyl alcohol NF
• Cetylic alcohol
• Cetylol
• Crodacol C
• Crodacol C70
• Crodacol C95 NF
• Crodacol-CAS
• Crodacol-CAT
• Dytol F-11
• Elfacos C
• Epal 16
• Epal 16NF
• Ethal
• Ethol
• Fancol CA
• Hexadecan-1-ol
• Hyfatol 16
• Hyfatol 16-95
• Kalcol 6098
• Lanette 16
• Lanol C
• Laurex 16
• Lipocol C
• Lorol 24
• Lorol C16
• LorolL 24
• Loxanol K
• Loxanol K extra
• Loxanwachs SK
• Palmitic alcohol
• Palmityl alcohol
• Philcohol 1600
• Product 308
• Rita CA
• Siponol CC
• Siponol wax-A
• cetanol
• cetyl alcohol
• hexadecanol
• hexadecyl alcohol
• n-1-Hexadecanol
• n-Hexadecan-1-ol
• n-Hexadecanol
• n-Hexadecyl alcohol
• n-cetyl alcohol

• ω : Acentric Factor.
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (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).
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_boil(P) : Boiling point at given pressure (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).
• Z_c : Critical Compressibility.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.7788; 1.0180]
ω	0.8156		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.7788		ChemSep v8.3 pure component data Compiled value
ω	1.0180		KDB
μ	1.67	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	-49.64	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-521.80	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfusH°	[56.40; 107.70]	kJ/mol
ΔfusH°	56.40	kJ/mol	Solid-Liquid Equilibrium of Binary Systems Containing Fatty Acids and Fatty Alcohols Using Differential Scanning Calorimetry
ΔfusH°	107.70	kJ/mol	Evaluation of the Vaporization, Fusion, and Sublimation Enthalpies of the 1-Alkanols: The Vaporization Enthalpy of 1-, 6-, 7-, and 9-Heptadecanol, 1-Octadecanol, 1-Eicosanol, 1-Docosanol, 1-Hexacosanol, and Cholesterol at T ) 298.15 K by Correlation Gas Chromatography
ΔvapH°	112.87	kJ/mol	Relay (1.0) Calculated Property
IE	10.02	eV	Relay (1.0) Calculated Property
log10WS	[-7.26; -7.00]
log10WS	-7.26		Aq. Solubility Prediction
log10WS	-7.00		Estimated Solubility
logPoct/wat	5.460		Crippen Calculated Property
McVol	242.170	ml/mol	McGowan Calculated Property
Pc	[1460.09; 1610.00]	kPa
Pc	1460.09	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	1468.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	1610.00	kPa	KDB
Ptriple	5.40e-05	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[1881.00; 1882.00]
Inp	1882.00		NIST
Inp	1881.00		NIST
Inp	1882.00		NIST
Tboil	[598.00; 607.00]	K
Tboil	598.00	K	ChemSep v8.3 pure component data Compiled value
Tboil	607.00	K	KDB
Tc	[768.60; 770.00]	K
Tc	770.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	768.60	K	ChemSep v8.3 pure component data Compiled value
Tc	770.00	K	KDB
Tfus	[321.15; 324.23]	K
Tfus	322.20	K	Phase diagrams of binary systems containing n-alkanes, or cyclohexane, or 1-alkanols and 2,3-pentanedione at atmospheric and high pressure
Tfus	322.91	K	Thermodynamics of organic mixtures containing amines. VIII. Systems with quinoline
Tfus	321.15	K	The manufacture of organic carbonate-poly(methyl ethylacrylate) nanowebs with thermal buffering effect
Tfus	322.20	K	High Pressure Solid-Liquid Equilibrium of Fatty Alcohols Binary Systems from 1-Dodecanol, 1-Tetradecanol, 1-Hexadecanol, and 1-Octadecanol
Tfus	322.65	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	322.35	K	ChemSep v8.3 pure component data Compiled value
Tfus	322.40	K	KDB
Tfus	Outlier 324.23	K	Aq. Solubility Prediction
Ttriple	322.35	K	ChemSep v8.3 pure component data Compiled value
UQi	10.15		ChemSep v8.3 pure component data Compiled value
URi	12.02		ChemSep v8.3 pure component data Compiled value
Vc	[0.937; 1.080]	m3/kmol
Vc	0.937	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	1.080	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.951	m3/kmol	KDB
Zc	[0.2390290; 0.2480000]
Zc	0.2480000		ChemSep v8.3 pure component data Compiled value
Zc	0.2390290		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
ΔvapH	73.35	kJ/mol	617.20	KDB

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboil(P)	465.70	K	2.02	Vapor-liquid equilibria of monoacylglicerol + monoacylglicerol or alcohol or fatty acid at subatmospheric pressures

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[379.58; 955.84]	J/mol×K	[298.15; 1500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + B·((C/T)/sinh(C/T))² + D·((E/T)/cosh(E/T))² Y is Cp,gas in J/mol×K, T in K
Coefficient A			2.63100e+02
Coefficient B			8.11370e+02
Coefficient C			1.50220e+03
Coefficient D			5.88800e+02
Coefficient E			7.08000e+02
Temperature range, min.			298.15
Temperature range, max.			1500.00
Cp,gas	379.58	J/mol×K	298.15	Calculated Property
Cp,gas	521.86	J/mol×K	431.69	Calculated Property
Cp,gas	634.81	J/mol×K	565.23	Calculated Property
Cp,gas	721.13	J/mol×K	698.77	Calculated Property
Cp,gas	787.69	J/mol×K	832.31	Calculated Property
Cp,gas	839.27	J/mol×K	965.84	Calculated Property
Cp,gas	879.44	J/mol×K	1099.38	Calculated Property
Cp,gas	910.95	J/mol×K	1232.92	Calculated Property
Cp,gas	935.89	J/mol×K	1366.46	Calculated Property
Cp,gas	955.84	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[605.97; 789.84]	J/mol×K	[322.35; 598.00]	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			-2.23060e+03
Coefficient B			1.82870e+01
Coefficient C			-3.79660e-02
Coefficient D			2.64750e-05
Coefficient E			0.00000e+00
Temperature range, min.			322.35
Temperature range, max.			598.00
Cp,liquid	605.97	J/mol×K	322.35	Calculated Property
Cp,liquid	658.33	J/mol×K	352.98	Calculated Property
Cp,liquid	692.06	J/mol×K	383.61	Calculated Property
Cp,liquid	711.72	J/mol×K	414.23	Calculated Property
Cp,liquid	721.87	J/mol×K	444.86	Calculated Property
Cp,liquid	727.09	J/mol×K	475.49	Calculated Property
Cp,liquid	731.93	J/mol×K	506.12	Calculated Property
Cp,liquid	740.96	J/mol×K	536.74	Calculated Property
Cp,liquid	758.74	J/mol×K	567.37	Calculated Property
Cp,liquid	789.84	J/mol×K	598.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0117994; 0.0002293]	Pa×s	[322.35; 598.00]	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			-6.96310e+01
Coefficient B			6.19560e+03
Coefficient C			7.95950e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			322.35
Temperature range, max.			598.00
η	0.0117994	Pa×s	322.35	Calculated Property
η	0.0045850	Pa×s	352.98	Calculated Property
η	0.0021895	Pa×s	383.61	Calculated Property
η	0.0012225	Pa×s	414.23	Calculated Property
η	0.0007702	Pa×s	444.86	Calculated Property
η	0.0005336	Pa×s	475.49	Calculated Property
η	0.0003986	Pa×s	506.12	Calculated Property
η	0.0003164	Pa×s	536.74	Calculated Property
η	0.0002639	Pa×s	567.37	Calculated Property
η	0.0002293	Pa×s	598.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[102.49; 0.00]	kJ/mol	[322.35; 768.60]	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			1.10640e+02
Coefficient B			-1.06250e+00
Coefficient C			3.94790e+00
Coefficient D			-2.57260e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			7.68600e+02
Temperature range, min.			322.35
Temperature range, max.			768.60
ΔvapH	102.49	kJ/mol	322.35	Calculated Property
ΔvapH	94.06	kJ/mol	371.93	Calculated Property
ΔvapH	85.19	kJ/mol	421.52	Calculated Property
ΔvapH	76.35	kJ/mol	471.10	Calculated Property
ΔvapH	67.91	kJ/mol	520.68	Calculated Property
ΔvapH	60.10	kJ/mol	570.27	Calculated Property
ΔvapH	53.00	kJ/mol	619.85	Calculated Property
ΔvapH	46.39	kJ/mol	669.43	Calculated Property
ΔvapH	39.12	kJ/mol	719.02	Calculated Property
ΔvapH	0.00	kJ/mol	768.60	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.66]	kPa	[464.78; 649.14]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.50566e+01
Coefficient B			-5.28146e+03
Coefficient C			-1.07180e+02
Temperature range, min.			464.78
Temperature range, max.			649.14
Pvap	1.33	kPa	464.78	Calculated Property
Pvap	2.97	kPa	485.26	Calculated Property
Pvap	6.08	kPa	505.75	Calculated Property
Pvap	11.63	kPa	526.23	Calculated Property
Pvap	20.92	kPa	546.72	Calculated Property
Pvap	35.72	kPa	567.20	Calculated Property
Pvap	58.28	kPa	587.69	Calculated Property
Pvap	91.34	kPa	608.17	Calculated Property
Pvap	138.20	kPa	628.66	Calculated Property
Pvap	202.66	kPa	649.14	Calculated Property
Pvap	[5.38e-05; 1463.31]	kPa	[322.35; 768.60]	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			1.79282e+02
Coefficient B			-1.95230e+04
Coefficient C			-2.22580e+01
Coefficient D			6.31450e-18
Coefficient E			6.00000e+00
Temperature range, min.			322.35
Temperature range, max.			768.60
Pvap	5.38e-05	kPa	322.35	Calculated Property
Pvap	7.22e-03	kPa	371.93	Calculated Property
Pvap	0.22	kPa	421.52	Calculated Property
Pvap	2.49	kPa	471.10	Calculated Property
Pvap	14.68	kPa	520.68	Calculated Property
Pvap	55.31	kPa	570.27	Calculated Property
Pvap	153.97	kPa	619.85	Calculated Property
Pvap	353.16	kPa	669.43	Calculated Property
Pvap	729.12	kPa	719.02	Calculated Property
Pvap	1463.31	kPa	768.60	Calculated Property
Pvap	[5.25e-05; 1689.08]	kPa	[322.35; 761.00]	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			3.18319e+02
Coefficient B			-2.59164e+04
Coefficient C			-4.32052e+01
Coefficient D			1.69556e-05
Coefficient E			0.00000e+00
Temperature range, min.			322.35
Temperature range, max.			761.00
Pvap	5.25e-05	kPa	322.35	Calculated Property
Pvap	8.18e-03	kPa	371.09	Calculated Property
Pvap	0.25	kPa	419.83	Calculated Property
Pvap	2.81	kPa	468.57	Calculated Property
Pvap	16.19	kPa	517.31	Calculated Property
Pvap	60.52	kPa	566.04	Calculated Property
Pvap	170.70	kPa	614.78	Calculated Property
Pvap	402.05	kPa	663.52	Calculated Property
Pvap	848.75	kPa	712.26	Calculated Property
Pvap	1689.08	kPa	761.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[815.79; 224.48]	kg/m3	[322.35; 768.60]	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			5.00253e+01
Coefficient B			2.22850e-01
Coefficient C			7.68600e+02
Coefficient D			2.78410e-01
Temperature range, min.			322.35
Temperature range, max.			768.60
ρl	815.79	kg/m3	322.35	Calculated Property
ρl	782.53	kg/m3	371.93	Calculated Property
ρl	747.67	kg/m3	421.52	Calculated Property
ρl	710.82	kg/m3	471.10	Calculated Property
ρl	671.40	kg/m3	520.68	Calculated Property
ρl	628.53	kg/m3	570.27	Calculated Property
ρl	580.64	kg/m3	619.85	Calculated Property
ρl	524.62	kg/m3	669.43	Calculated Property
ρl	452.01	kg/m3	719.02	Calculated Property
ρl	224.48	kg/m3	768.60	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.00]	N/m	[322.35; 768.60]	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			5.89810e-02
Coefficient B			1.31380e+00
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			7.68600e+02
Temperature range, min.			322.35
Temperature range, max.			768.60
γ	0.03	N/m	322.35	Calculated Property
γ	0.02	N/m	371.93	Calculated Property
γ	0.02	N/m	421.52	Calculated Property
γ	0.02	N/m	471.10	Calculated Property
γ	0.01	N/m	520.68	Calculated Property
γ	0.01	N/m	570.27	Calculated Property
γ	0.01	N/m	619.85	Calculated Property
γ	0.00	N/m	669.43	Calculated Property
γ	0.00	N/m	719.02	Calculated Property
γ	0.00	N/m	768.60	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.03; 0.08]	W/m×K	[598.00; 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			-1.49400e+00
Coefficient B			-1.16870e-03
Coefficient C			-2.43610e+03
Coefficient D			-1.81540e+07
Temperature range, min.			598.00
Temperature range, max.			1000.00
λgas	0.03	W/m×K	598.00	Calculated Property
λgas	0.03	W/m×K	642.67	Calculated Property
λgas	0.04	W/m×K	687.33	Calculated Property
λgas	0.04	W/m×K	732.00	Calculated Property
λgas	0.05	W/m×K	776.67	Calculated Property
λgas	0.05	W/m×K	821.33	Calculated Property
λgas	0.06	W/m×K	866.00	Calculated Property
λgas	0.06	W/m×K	910.67	Calculated Property
λgas	0.07	W/m×K	955.33	Calculated Property
λgas	0.08	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.14; 0.07]	W/m×K	[322.35; 598.00]	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			2.20810e-01
Coefficient B			-2.50000e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			322.35
Temperature range, max.			598.00
λliquid	0.14	W/m×K	322.35	Calculated Property
λliquid	0.13	W/m×K	352.98	Calculated Property
λliquid	0.12	W/m×K	383.61	Calculated Property
λliquid	0.12	W/m×K	414.23	Calculated Property
λliquid	0.11	W/m×K	444.86	Calculated Property
λliquid	0.10	W/m×K	475.49	Calculated Property
λliquid	0.09	W/m×K	506.12	Calculated Property
λliquid	0.09	W/m×K	536.74	Calculated Property
λliquid	0.08	W/m×K	567.37	Calculated Property
λliquid	0.07	W/m×K	598.00	Calculated Property

Similar Compounds

Find more compounds similar to 1-Hexadecanol.

Mixtures

• Quinoline + 1-Hexadecanol
• Propane + 1-Hexadecanol
• 1-Hexadecanol + 2,3-Pentadione
• 1-Hexadecanol + 1-Decanol
• 1-Hexadecanol + 1-Octadecanol
• 1-Hexadecanol + Methyl tetradecanoate
• 1-Dodecanol + 1-Hexadecanol
• 1-Hexadecanol + 1-Tetradecanol
• Carbon dioxide + 1-Hexadecanol
• Octadecanoic acid + 1-Hexadecanol

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).
• 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.
• Cheméo Relay (1.0)
• 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
• Phase diagrams of binary systems containing n-alkanes, or cyclohexane, or 1-alkanols and 2,3-pentanedione at atmospheric and high pressure
• Phase equilibria of high molecular mass 1-alcohols in supercritical propane
• The solid-liquid phase diagrams of binary mixtures of even saturated fatty alcohols
• Vapor-liquid equilibria of monoacylglicerol + monoacylglicerol or alcohol or fatty acid at subatmospheric pressures
• Thermodynamics of organic mixtures containing amines. VIII. Systems with quinoline
• The manufacture of organic carbonate-poly(methyl ethylacrylate) nanowebs with thermal buffering effect
• High Pressure Solid-Liquid Equilibrium of Fatty Alcohols Binary Systems from 1-Dodecanol, 1-Tetradecanol, 1-Hexadecanol, and 1-Octadecanol
• High Pressure Phase Behavior of the Homologous Series CO2 + 1-Alcohols
• Vapor-Liquid Equilibria of Binary Systems with Long-Chain Organic Compounds (Fatty Alcohol, Fatty Ester, Acylglycerol, and n-Paraffin) at Subatmospheric Pressures
• Solid-Liquid Equilibrium of Binary Systems Containing Fatty Acids and Fatty Alcohols Using Differential Scanning Calorimetry
• Determination of Partitioning Coefficients of Numerous Organic Solutes between a Long-Chain Aliphatic Alcohol and the Gas Phase as a Function of Temperature
• Evaluation of the Vaporization, Fusion, and Sublimation Enthalpies of the 1-Alkanols: The Vaporization Enthalpy of 1-, 6-, 7-, and 9-Heptadecanol, 1-Octadecanol, 1-Eicosanol, 1-Docosanol, 1-Hexacosanol, and Cholesterol at T ) 298.15 K by Correlation Gas Chromatography
• Liquid-Liquid Phase Behavior of Solutions of 1-Dodecyl-3-methylimidazolium Bis(trifluoromethylsulphonyl)imide (C12mimNTf2) in n- Alkyl Alcohols
• Liquid-Liquid Phase Behavior of Solutions of 1-Octyl- and 1-Decyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide (C8,10mimNTf2) in n-Alkyl Alcohols
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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