Chemical Properties of 1-Hexanol (CAS 111-27-3)

InChI

InChI=1S/C6H14O/c1-2-3-4-5-6-7/h7H,2-6H2,1H3

InChI Key

ZSIAUFGUXNUGDI-UHFFFAOYSA-N

Formula

C6H14O

SMILES

CCCCCCO

Molecular Weight¹

102.17

CAS

111-27-3

Other Names

• 1-Hexyl alcohol
• 1-hydroxyhexane
• Caproyl alcohol
• Epal 6
• Hexanol
• Hexanol-(1)
• NSC 9254
• amylcarbinol
• hexan-1-ol
• hexyl alcohol
• n-C6H13OH
• n-Hexan-1-ol
• n-hexanol
• n-hexyl alcohol
• pentylcarbinol

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• T_ig : Autoignition Temperature (K).
• α_p : Isobaric thermal expansion coefficient (1/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).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• ε_r : Dielectric Constant (Relative permittivity).
• LFL : Lower Flammability Limit (% in Air).
• UFL : Upper Flammability Limit (% in Air).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• T_flash,oc : Flash Point (Open Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• 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).
• ν : Kinematic viscosity (m²/s).
• 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.
• NFPA Safety : NFPA Safety 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°_gas : Molar entropy at standard conditions (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• c_sound,fluid : Speed of sound in fluid (m/s).
• 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).
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Contents

1. Physical Properties
2. Temperature Dependent Properties
3. Datasets
4. Correlations
5. Similar Compounds
6. Mixtures
7. Sources

Physical Properties

Property	Value	Unit	Source
ω	[0.5600; 0.5800]
ω	0.5600		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.5800		ChemSep v8.3 pure component data Compiled value
ω	0.5600		KDB
PAff	799.00	kJ/mol	NIST
Tig	577.59	K	KDB
ΔcH°liquid	[-3984.37; -3978.10]	kJ/mol
ΔcH°liquid	-3984.37 ± 0.44	kJ/mol	NIST
ΔcH°liquid	-3982.60 ± 0.92	kJ/mol	NIST
ΔcH°liquid	-3978.10 ± 2.00	kJ/mol	NIST
ΔcH°liquid	-3978.10	kJ/mol	NIST
μ	[1.65; 1.80]	debye
μ	1.65	debye	ChemSep v8.3 pure component data Compiled value
μ	1.80	debye	KDB
η	[0.0044395; 0.0052910]	Pa×s
η	0.0052910	Pa×s	Studies on Transport and Thermodynamic Properties of Binary Mixtures of Hexan-1-ol with Halogenated Compounds at 293.15 K
η	0.0044395	Pa×s	Volumetric and Viscometric Properties of Binary Liquid Mixtures of Ethylene Glycol Monomethyl Ether + 1-Hexanol, 1-Octanol, and 1-Decanol at Temperatures of T = (293.15, 298.15, 303.15, and 308.15) K
εr	13.30		NCMS SOLV-DB
LFL	1.20	% in Air	KDB
UFL	7.70	% in Air	KDB
Tflash,cc	[335.15; 338.15]	K
Tflash,cc	338.15	K	KDB
Tflash,cc	335.15	K	NCMS SOLV-DB
Tflash,oc	335.93	K	KDB
ΔfG°	[-135.70; -134.40]	kJ/mol
ΔfG°	-134.40	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	-135.70	kJ/mol	KDB
ΔfH°gas	[-325.80; -308.30]	kJ/mol
ΔfH°gas	-318.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-317.80	kJ/mol	KDB
ΔfH°gas	-308.30	kJ/mol	NIST
ΔfH°gas	-315.60 ± 0.50	kJ/mol	NIST
ΔfH°gas	-310.20	kJ/mol	NIST
ΔfH°gas	-317.50 ± 1.00	kJ/mol	NIST
ΔfH°gas	-314.70 ± 1.40	kJ/mol	NIST
ΔfH°gas	-318.50	kJ/mol	NIST
ΔfH°gas	-325.80 ± 4.00	kJ/mol	NIST
ΔfH°liquid	[-387.70; -377.50]	kJ/mol
ΔfH°liquid	-377.50 ± 0.44	kJ/mol	NIST
ΔfH°liquid	-379.40 ± 1.00	kJ/mol	NIST
ΔfH°liquid	-383.90 ± 2.00	kJ/mol	NIST
ΔfH°liquid	-387.70	kJ/mol	NIST
ΔfusH°	16.73	kJ/mol	Heat Capacities and Derived Thermodynamic Functions of 1-Hexanol, 1-Heptanol, 1-Octanol, and 1-Decanol between 5 K and 390 K
ΔvapH°	[59.10; 69.20]	kJ/mol
ΔvapH°	61.84	kJ/mol	NCMS SOLV-DB
ΔvapH°	61.61	kJ/mol	NIST
ΔvapH°	59.10	kJ/mol	NIST
ΔvapH°	59.90	kJ/mol	NIST
ΔvapH°	61.70 ± 0.30	kJ/mol	NIST
ΔvapH°	61.10	kJ/mol	NIST
ΔvapH°	62.10 ± 0.20	kJ/mol	NIST
ΔvapH°	61.50	kJ/mol	NIST
ΔvapH°	61.60	kJ/mol	NIST
ΔvapH°	61.85 ± 0.20	kJ/mol	NIST
ΔvapH°	60.80 ± 0.20	kJ/mol	NIST
ΔvapH°	61.60 ± 0.20	kJ/mol	NIST
ΔvapH°	61.60 ± 0.20	kJ/mol	NIST
ΔvapH°	62.80 ± 1.30	kJ/mol	NIST
ΔvapH°	Outlier 69.20	kJ/mol	NIST
IE	[9.89; 10.35]	eV
IE	9.89	eV	NIST
IE	10.35	eV	NIST
log10WS	[-1.24; -1.24]
log10WS	-1.24		Aq. Solubility Prediction
log10WS	-1.24		Estimated Solubility
logPoct/wat	2.030		NCMS SOLV-DB
McVol	101.270	ml/mol	McGowan Calculated Property
NFPA Fire	[%!d(float64=2); %!d(float64=2)]
NFPA Fire	2		KDB
NFPA Fire	2		NCMS SOLV-DB
NFPA Health	[%!d(float64=1); %!d(float64=1)]
NFPA Health	1		KDB
NFPA Health	1		NCMS SOLV-DB
NFPA Safety	0		NCMS SOLV-DB
Pc	[3413.00; 3510.00]	kPa
Pc	3417.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Pc	3419.72	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	Outlier 3510.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	3417.00	kPa	KDB
Pc	3420.00 ± 20.00	kPa	NIST
Pc	3420.00 ± 50.00	kPa	NIST
Pc	3413.00 ± 6.00	kPa	NIST
Pc	3413.00 ± 20.00	kPa	NIST
Ptriple	2.95e-05	kPa	ChemSep v8.3 pure component data Compiled value
ρc	[259.52; 267.70]	kg/m3
ρc	263.61 ± 2.04	kg/m3	NIST
ρc	267.70	kg/m3	NIST
ρc	259.52 ± 6.13	kg/m3	NIST
ρc	267.70 ± 3.07	kg/m3	NIST
Inp	[136.97; 896.80]
Inp	889.40		NIST
Inp	896.80		NIST
Inp	870.10		NIST
Inp	866.30		NIST
Inp	862.30		NIST
Inp	861.10		NIST
Inp	859.90		NIST
Inp	859.54		NIST
Inp	848.00		NIST
Inp	848.20		NIST
Inp	831.90		NIST
Inp	836.60		NIST
Inp	878.00		NIST
Inp	879.50		NIST
Inp	822.00		NIST
Inp	851.00		NIST
Inp	845.00		NIST
Inp	823.00		NIST
Inp	863.00		NIST
Inp	860.00		NIST
Inp	854.00		NIST
Inp	852.00		NIST
Inp	831.00		NIST
Inp	838.00		NIST
Inp	856.00		NIST
Inp	853.00		NIST
Inp	850.00		NIST
Inp	831.20		NIST
Inp	831.00		NIST
Inp	855.00		NIST
Inp	856.00		NIST
Inp	832.00		NIST
Inp	862.00		NIST
Inp	821.00		NIST
Inp	854.00		NIST
Inp	867.00		NIST
Inp	869.00		NIST
Inp	856.00		NIST
Inp	860.00		NIST
Inp	878.00		NIST
Inp	860.00		NIST
Inp	859.00		NIST
Inp	868.00		NIST
Inp	868.00		NIST
Inp	867.00		NIST
Inp	881.00		NIST
Inp	881.00		NIST
Inp	858.00		NIST
Inp	859.00		NIST
Inp	857.00		NIST
Inp	858.00		NIST
Inp	858.00		NIST
Inp	858.00		NIST
Inp	858.00		NIST
Inp	858.00		NIST
Inp	853.00		NIST
Inp	865.00		NIST
Inp	858.00		NIST
Inp	850.00		NIST
Inp	865.00		NIST
Inp	868.00		NIST
Inp	867.00		NIST
Inp	867.00		NIST
Inp	864.00		NIST
Inp	862.00		NIST
Inp	854.00		NIST
Inp	865.00		NIST
Inp	867.00		NIST
Inp	852.00		NIST
Inp	871.00		NIST
Inp	871.00		NIST
Inp	870.00		NIST
Inp	867.00		NIST
Inp	880.00		NIST
Inp	880.00		NIST
Inp	876.00		NIST
Inp	862.00		NIST
Inp	867.00		NIST
Inp	867.00		NIST
Inp	884.00		NIST
Inp	867.00		NIST
Inp	867.00		NIST
Inp	867.00		NIST
Inp	874.00		NIST
Inp	874.00		NIST
Inp	867.00		NIST
Inp	841.00		NIST
Inp	847.90		NIST
Inp	865.10		NIST
Inp	885.00		NIST
Inp	872.00		NIST
Inp	867.00		NIST
Inp	843.00		NIST
Inp	869.00		NIST
Inp	849.00		NIST
Inp	849.00		NIST
Inp	863.00		NIST
Inp	867.00		NIST
Inp	860.00		NIST
Inp	854.00		NIST
Inp	854.00		NIST
Inp	854.00		NIST
Inp	876.00		NIST
Inp	880.00		NIST
Inp	852.00		NIST
Inp	849.00		NIST
Inp	860.00		NIST
Inp	866.00		NIST
Inp	867.00		NIST
Inp	859.00		NIST
Inp	861.00		NIST
Inp	869.00		NIST
Inp	863.00		NIST
Inp	852.70		NIST
Inp	854.00		NIST
Inp	880.00		NIST
Inp	857.00		NIST
Inp	869.00		NIST
Inp	870.00		NIST
Inp	859.00		NIST
Inp	861.00		NIST
Inp	851.00		NIST
Inp	853.00		NIST
Inp	854.00		NIST
Inp	854.00		NIST
Inp	867.00		NIST
Inp	852.00		NIST
Inp	852.00		NIST
Inp	859.00		NIST
Inp	861.00		NIST
Inp	859.00		NIST
Inp	859.00		NIST
Inp	866.00		NIST
Inp	858.00		NIST
Inp	889.00		NIST
Inp	869.00		NIST
Inp	860.00		NIST
Inp	848.00		NIST
Inp	857.00		NIST
Inp	861.00		NIST
Inp	859.00		NIST
Inp	867.00		NIST
Inp	872.00		NIST
Inp	869.00		NIST
Inp	865.60		NIST
Inp	828.00		NIST
Inp	828.00		NIST
Inp	867.00		NIST
Inp	884.00		NIST
Inp	876.00		NIST
Inp	853.00		NIST
Inp	876.00		NIST
Inp	865.00		NIST
Inp	863.00		NIST
Inp	872.00		NIST
Inp	870.00		NIST
Inp	871.00		NIST
Inp	876.00		NIST
Inp	876.00		NIST
Inp	867.00		NIST
Inp	871.00		NIST
Inp	867.00		NIST
Inp	871.00		NIST
Inp	888.00		NIST
Inp	873.00		NIST
Inp	868.00		NIST
Inp	874.00		NIST
Inp	868.00		NIST
Inp	848.00		NIST
Inp	851.00		NIST
Inp	849.00		NIST
Inp	856.00		NIST
Inp	868.00		NIST
Inp	853.00		NIST
Inp	890.00		NIST
Inp	870.00		NIST
Inp	871.00		NIST
Inp	876.00		NIST
Inp	874.00		NIST
Inp	852.00		NIST
Inp	865.00		NIST
Inp	868.00		NIST
Inp	861.00		NIST
Inp	863.00		NIST
Inp	874.00		NIST
Inp	870.00		NIST
Inp	867.00		NIST
Inp	863.00		NIST
Inp	860.00		NIST
Inp	860.00		NIST
Inp	868.00		NIST
Inp	873.00		NIST
Inp	875.00		NIST
Inp	839.00		NIST
Inp	868.00		NIST
Inp	871.00		NIST
Inp	878.00		NIST
Inp	879.00		NIST
Inp	843.00		NIST
Inp	868.00		NIST
Inp	868.00		NIST
Inp	878.00		NIST
Inp	871.00		NIST
Inp	871.00		NIST
Inp	870.00		NIST
Inp	870.00		NIST
Inp	859.00		NIST
Inp	847.00		NIST
Inp	845.00		NIST
Inp	887.00		NIST
Inp	866.00		NIST
Inp	872.00		NIST
Inp	882.00		NIST
Inp	888.00		NIST
Inp	878.10		NIST
Inp	855.00		NIST
Inp	832.00		NIST
Inp	867.00		NIST
Inp	858.00		NIST
Inp	872.00		NIST
Inp	850.00		NIST
Inp	862.00		NIST
Inp	862.00		NIST
Inp	864.00		NIST
Inp	878.00		NIST
Inp	865.00		NIST
Inp	885.00		NIST
Inp	866.00		NIST
Inp	859.00		NIST
Inp	847.00		NIST
Inp	878.00		NIST
Inp	866.00		NIST
Inp	843.00		NIST
Inp	839.00		NIST
Inp	858.00		NIST
Inp	858.00		NIST
Inp	858.00		NIST
Inp	859.00		NIST
Inp	866.00		NIST
Inp	867.00		NIST
Inp	852.00		NIST
Inp	859.00		NIST
Inp	868.00		NIST
Inp	849.00		NIST
Inp	868.00		NIST
Inp	872.00		NIST
Inp	872.00		NIST
Inp	848.00		NIST
Inp	867.00		NIST
Inp	859.11		NIST
Inp	888.00		NIST
Inp	855.00		NIST
Inp	867.00		NIST
Inp	874.00		NIST
Inp	877.00		NIST
Inp	854.00		NIST
Inp	849.00		NIST
Inp	871.00		NIST
Inp	848.00		NIST
Inp	862.00		NIST
Inp	858.00		NIST
Inp	870.00		NIST
Inp	878.00		NIST
Inp	849.00		NIST
Inp	850.00		NIST
Inp	850.00		NIST
Inp	851.00		NIST
Inp	852.00		NIST
Inp	848.00		NIST
Inp	862.00		NIST
Inp	872.00		NIST
Inp	858.00		NIST
Inp	848.00		NIST
Inp	848.00		NIST
Inp	846.00		NIST
Inp	848.00		NIST
Inp	849.00		NIST
Inp	848.00		NIST
Inp	847.00		NIST
Inp	867.00		NIST
Inp	856.00		NIST
Inp	856.00		NIST
Inp	852.00		NIST
Inp	849.00		NIST
Inp	864.00		NIST
Inp	859.00		NIST
Inp	858.00		NIST
Inp	862.00		NIST
Inp	874.00		NIST
Inp	888.00		NIST
Inp	863.00		NIST
Inp	872.00		NIST
Inp	863.00		NIST
Inp	876.00		NIST
Inp	857.00		NIST
Inp	874.00		NIST
Inp	867.00		NIST
Inp	857.00		NIST
Inp	871.00		NIST
Inp	872.00		NIST
Inp	860.00		NIST
Inp	872.00		NIST
Inp	861.00		NIST
Inp	869.00		NIST
Inp	876.00		NIST
Inp	889.00		NIST
Inp	888.00		NIST
Inp	861.00		NIST
Inp	850.00		NIST
Inp	854.00		NIST
Inp	837.00		NIST
Inp	871.00		NIST
Inp	869.00		NIST
Inp	860.00		NIST
Inp	871.00		NIST
Inp	886.00		NIST
Inp	888.00		NIST
Inp	849.00		NIST
Inp	865.00		NIST
Inp	872.00		NIST
Inp	870.00		NIST
Inp	853.00		NIST
Inp	864.00		NIST
Inp	872.00		NIST
Inp	868.00		NIST
Inp	871.00		NIST
Inp	864.00		NIST
Inp	864.00		NIST
Inp	867.00		NIST
Inp	867.00		NIST
Inp	878.00		NIST
Inp	865.00		NIST
Inp	852.00		NIST
Inp	883.00		NIST
Inp	878.00		NIST
Inp	871.00		NIST
Inp	850.00		NIST
Inp	867.00		NIST
Inp	858.00		NIST
Inp	867.00		NIST
Inp	856.00		NIST
Inp	870.00		NIST
Inp	870.00		NIST
Inp	852.00		NIST
Inp	858.00		NIST
Inp	827.00		NIST
Inp	866.00		NIST
Inp	870.00		NIST
Inp	853.00		NIST
Inp	858.00		NIST
Inp	865.80		NIST
Inp	870.00		NIST
Inp	844.00		NIST
Inp	891.00		NIST
Inp	875.00		NIST
Inp	853.00		NIST
Inp	842.00		NIST
Inp	852.00		NIST
Inp	862.00		NIST
Inp	843.00		NIST
Inp	854.00		NIST
Inp	871.00		NIST
Inp	852.00		NIST
Inp	857.00		NIST
Inp	858.00		NIST
Inp	858.00		NIST
Inp	852.00		NIST
Inp	860.00		NIST
Inp	848.00		NIST
Inp	868.00		NIST
Inp	858.00		NIST
Inp	858.00		NIST
Inp	839.00		NIST
Inp	858.00		NIST
Inp	885.00		NIST
Inp	856.00		NIST
Inp	858.00		NIST
Inp	884.00		NIST
Inp	Outlier 136.97		NIST
Inp	858.00		NIST
Inp	874.00		NIST
Inp	876.00		NIST
Inp	871.00		NIST
Inp	869.00		NIST
Inp	850.00		NIST
Inp	860.00		NIST
Inp	865.00		NIST
Inp	872.00		NIST
Inp	867.00		NIST
Inp	883.00		NIST
Inp	852.00		NIST
Inp	853.00		NIST
Inp	891.00		NIST
Inp	862.00		NIST
Inp	857.00		NIST
Inp	848.00		NIST
Inp	863.00		NIST
Inp	839.00		NIST
Inp	843.00		NIST
Inp	845.00		NIST
Inp	888.00		NIST
Inp	864.00		NIST
Inp	859.00		NIST
Inp	866.00		NIST
Inp	849.00		NIST
Inp	847.00		NIST
Inp	Outlier 136.97		NIST
Inp	880.00		NIST
Inp	865.10		NIST
Inp	852.70		NIST
Inp	870.00		NIST
Inp	854.00		NIST
Ip	[1308.00; 1398.00]
Ip	1384.00		NIST
Ip	1384.00		NIST
Ip	1357.00		NIST
Ip	1332.00		NIST
Ip	1362.00		NIST
Ip	1378.00		NIST
Ip	1358.00		NIST
Ip	1348.00		NIST
Ip	1347.99		NIST
Ip	1346.20		NIST
Ip	1344.79		NIST
Ip	1348.98		NIST
Ip	Outlier 1315.00		NIST
Ip	1329.00		NIST
Ip	1326.00		NIST
Ip	1357.00		NIST
Ip	1350.00		NIST
Ip	Outlier 1321.00		NIST
Ip	1342.00		NIST
Ip	1355.00		NIST
Ip	1342.00		NIST
Ip	1350.00		NIST
Ip	1338.00		NIST
Ip	1347.00		NIST
Ip	1342.00		NIST
Ip	1339.00		NIST
Ip	Outlier 1316.00		NIST
Ip	Outlier 1316.00		NIST
Ip	1339.00		NIST
Ip	1357.00		NIST
Ip	1359.00		NIST
Ip	1359.00		NIST
Ip	1356.00		NIST
Ip	1359.00		NIST
Ip	1376.00		NIST
Ip	1356.00		NIST
Ip	Outlier 1308.00		NIST
Ip	1332.00		NIST
Ip	1339.00		NIST
Ip	1337.00		NIST
Ip	1362.00		NIST
Ip	1361.00		NIST
Ip	1361.00		NIST
Ip	1360.00		NIST
Ip	1360.00		NIST
Ip	1363.00		NIST
Ip	1363.00		NIST
Ip	1340.00		NIST
Ip	1351.00		NIST
Ip	1353.00		NIST
Ip	1356.00		NIST
Ip	1359.00		NIST
Ip	1360.00		NIST
Ip	1345.00		NIST
Ip	1363.00		NIST
Ip	1348.00		NIST
Ip	1343.00		NIST
Ip	1348.00		NIST
Ip	1339.00		NIST
Ip	1344.00		NIST
Ip	Outlier 1320.00		NIST
Ip	1353.00		NIST
Ip	1367.00		NIST
Ip	1363.00		NIST
Ip	1362.00		NIST
Ip	1356.00		NIST
Ip	1371.00		NIST
Ip	1371.00		NIST
Ip	1371.00		NIST
Ip	1344.00		NIST
Ip	1344.00		NIST
Ip	Outlier 1320.00		NIST
Ip	1344.00		NIST
Ip	1371.00		NIST
Ip	1338.00		NIST
Ip	1362.00		NIST
Ip	1335.00		NIST
Ip	1354.00		NIST
Ip	Outlier 1396.00		NIST
Ip	1343.00		NIST
Ip	1354.00		NIST
Ip	1358.00		NIST
Ip	1358.00		NIST
Ip	1358.00		NIST
Ip	1360.60		NIST
Ip	1343.00		NIST
Ip	1358.00		NIST
Ip	Outlier 1392.00		NIST
Ip	1356.00		NIST
Ip	1356.00		NIST
Ip	1353.00		NIST
Ip	1336.00		NIST
Ip	1355.00		NIST
Ip	1368.00		NIST
Ip	Outlier 1315.00		NIST
Ip	1351.00		NIST
Ip	1355.00		NIST
Ip	1351.00		NIST
Ip	1353.00		NIST
Ip	1356.00		NIST
Ip	1355.00		NIST
Ip	1333.00		NIST
Ip	1335.00		NIST
Ip	1349.00		NIST
Ip	1354.00		NIST
Ip	1367.00		NIST
Ip	1364.00		NIST
Ip	1348.00		NIST
Ip	1338.00		NIST
Ip	1345.00		NIST
Ip	1345.00		NIST
Ip	1361.00		NIST
Ip	1358.00		NIST
Ip	1325.00		NIST
Ip	1361.00		NIST
Ip	1353.00		NIST
Ip	1343.00		NIST
Ip	1353.00		NIST
Ip	1336.00		NIST
Ip	1348.00		NIST
Ip	1353.00		NIST
Ip	1353.00		NIST
Ip	1353.00		NIST
Ip	1357.00		NIST
Ip	1345.00		NIST
Ip	1337.00		NIST
Ip	1354.00		NIST
Ip	1356.00		NIST
Ip	1359.00		NIST
Ip	1343.00		NIST
Ip	Outlier 1318.00		NIST
Ip	Outlier 1314.00		NIST
Ip	1324.00		NIST
Ip	1362.00		NIST
Ip	1354.00		NIST
Ip	1359.00		NIST
Ip	1362.00		NIST
Ip	1360.00		NIST
Ip	1351.00		NIST
Ip	1372.00		NIST
Ip	1345.00		NIST
Ip	1370.00		NIST
Ip	1357.00		NIST
Ip	1356.00		NIST
Ip	1356.00		NIST
Ip	1361.00		NIST
Ip	1336.00		NIST
Ip	1342.00		NIST
Ip	1371.00		NIST
Ip	1356.00		NIST
Ip	1351.00		NIST
Ip	1344.00		NIST
Ip	1368.00		NIST
Ip	1359.00		NIST
Ip	1359.00		NIST
Ip	1386.00		NIST
Ip	1339.00		NIST
Ip	1336.00		NIST
Ip	1360.00		NIST
Ip	Outlier 1387.00		NIST
Ip	1357.00		NIST
Ip	1348.00		NIST
Ip	1345.00		NIST
Ip	1375.00		NIST
Ip	1357.00		NIST
Ip	1353.00		NIST
Ip	1356.00		NIST
Ip	1341.00		NIST
Ip	1363.00		NIST
Ip	1360.00		NIST
Ip	Outlier 1316.00		NIST
Ip	1357.00		NIST
Ip	1363.00		NIST
Ip	1363.00		NIST
Ip	1357.00		NIST
Ip	1348.00		NIST
Ip	1341.00		NIST
Ip	1341.00		NIST
Ip	1362.00		NIST
Ip	1350.00		NIST
Ip	1336.00		NIST
Ip	1352.00		NIST
Ip	Outlier 1321.00		NIST
Ip	1378.00		NIST
Ip	1367.00		NIST
Ip	1362.00		NIST
Ip	1346.00		NIST
Ip	Outlier 1311.00		NIST
Ip	1363.00		NIST
Ip	1341.00		NIST
Ip	1351.00		NIST
Ip	1353.00		NIST
Ip	1384.00		NIST
Ip	1379.00		NIST
Ip	Outlier 1398.00		NIST
Ip	1356.00		NIST
Ip	1356.00		NIST
Ip	1356.00		NIST
Ip	1362.00		NIST
Ip	1354.00		NIST
Ip	1349.00		NIST
Ip	1356.00		NIST
Ip	1358.00		NIST
Ip	1359.00		NIST
Ip	Outlier 1320.00		NIST
Ip	1357.00		NIST
Ip	1353.00		NIST
Ip	1350.00		NIST
Ip	1354.00		NIST
Ip	1354.00		NIST
Ip	Outlier 1392.00		NIST
Ip	1354.00		NIST
Ip	Outlier 1392.00		NIST
Ip	1386.00		NIST
Ip	1360.00		NIST
Ip	1350.00		NIST
Ip	1369.00		NIST
Ip	1374.00		NIST
Ip	1348.00		NIST
Ip	1348.00		NIST
Ip	1360.00		NIST
Ip	1360.00		NIST
Ip	1341.00		NIST
Ip	1352.00		NIST
Ip	1358.00		NIST
Ip	1341.00		NIST
Ip	Outlier 1316.00		NIST
Ip	1365.00		NIST
Ip	1359.00		NIST
Ip	1371.00		NIST
Ip	1325.00		NIST
Ip	1359.00		NIST
Ip	1357.00		NIST
Ip	1345.00		NIST
Ip	1366.00		NIST
Ip	1357.00		NIST
Ip	1360.00		NIST
Ip	Outlier 1320.00		NIST
Ip	1380.00		NIST
Ip	Outlier 1316.00		NIST
Ip	1353.00		NIST
Ip	1365.40		NIST
Ip	Outlier 1316.00		NIST
Ip	1352.00		NIST
Ip	1352.00		NIST
Ip	1349.00		NIST
Ip	1352.00		NIST
Ip	1366.00		NIST
Ip	1358.00		NIST
Ip	1361.00		NIST
Ip	Outlier 1321.00		NIST
Ip	1355.00		NIST
Ip	1371.00		NIST
Ip	1375.00		NIST
Ip	Outlier 1392.00		NIST
Ip	1361.00		NIST
Ip	1362.00		NIST
Ip	1354.00		NIST
Ip	1359.00		NIST
Ip	1361.00		NIST
Ip	1360.00		NIST
Ip	1366.00		NIST
Ip	1362.00		NIST
Ip	1360.00		NIST
Ip	1357.00		NIST
Ip	1340.00		NIST
Ip	1345.00		NIST
Ip	1366.00		NIST
Ip	1359.00		NIST
Ip	Outlier 1392.00		NIST
Ip	1366.00		NIST
Ip	1352.00		NIST
Ip	1336.00		NIST
Ip	Outlier 1392.00		NIST
Ip	1356.00		NIST
Ip	1345.00		NIST
Ip	Outlier 1392.00		NIST
Ip	1360.00		NIST
Ip	1354.00		NIST
Ip	1359.00		NIST
Ip	1331.00		NIST
Ip	1358.00		NIST
Ip	1356.00		NIST
Ip	Outlier 1392.00		NIST
Ip	1358.00		NIST
Ip	1346.00		NIST
Ip	1350.00		NIST
Ip	1362.00		NIST
Ip	1372.00		NIST
Ip	1360.00		NIST
Ip	1358.00		NIST
Ip	1356.00		NIST
Ip	1358.00		NIST
Ip	1360.00		NIST
Ip	1358.00		NIST
Ip	1368.00		NIST
Ip	1353.00		NIST
Ip	1343.00		NIST
Ip	1358.00		NIST
Ip	1362.00		NIST
Ip	Outlier 1316.00		NIST
Ip	1358.00		NIST
Ip	1373.00		NIST
Ip	1360.00		NIST
Ip	Outlier 1316.00		NIST
Ip	1360.00		NIST
Ip	1365.00		NIST
Ip	1363.00		NIST
Ip	1363.00		NIST
Ip	1348.00		NIST
Ip	1328.00		NIST
Ip	1354.00		NIST
Ip	1363.00		NIST
Ip	1363.00		NIST
Ip	1341.00		NIST
Ip	1336.00		NIST
Ip	1344.00		NIST
Ip	1365.00		NIST
Ip	Outlier 1316.00		NIST
Ip	1330.00		NIST
Ip	1347.00		NIST
Ip	1332.00		NIST
Ip	1332.00		NIST
Ip	1372.00		NIST
Ip	1354.00		NIST
Ip	1358.00		NIST
Ip	1360.00		NIST
Ip	1367.00		NIST
Ip	1352.00		NIST
Ip	Outlier 1316.00		NIST
Ip	1360.00		NIST
Ip	1375.00		NIST
Ip	1363.00		NIST
Ip	1362.00		NIST
Ip	1378.00		NIST
Ip	1379.00		NIST
Ip	1359.00		NIST
Ip	1354.00		NIST
Ip	1386.00		NIST
Ip	1348.00		NIST
Ip	1352.00		NIST
Ip	1345.00		NIST
Ip	1380.00		NIST
Ip	1358.00		NIST
Ip	1355.00		NIST
Ip	1366.00		NIST
Ip	Outlier 1392.00		NIST
Ip	1350.00		NIST
Ip	1356.00		NIST
Ip	1353.00		NIST
Ip	1365.00		NIST
Ip	1344.00		NIST
Ip	1332.00		NIST
Ip	1384.00		NIST
Ip	1344.79		NIST
Ip	1357.00		NIST
Ip	1342.00		NIST
Ip	1351.00		NIST
Ip	1339.00		NIST
Ip	1371.00		NIST
Ip	Outlier 1396.00		NIST
Ip	1368.00		NIST
Ip	1349.00		NIST
Ip	1338.00		NIST
Ip	1325.00		NIST
Ip	1336.00		NIST
S°gas	439.70 ± 2.10	J/mol×K	NIST
S°liquid	287.40	J/mol×K	NIST
Tboil	[409.15; 440.15]	K
Tboil	430.75	K	Excess molar volumes of ternary mixtures of 1,3-dichlorobenzene and methyl ethyl ketone with 1-alkanols at 303.15K
Tboil	430.50	K	Phase equilibria of (water + levunilic acid + alcohol) ternary systems
Tboil	430.11	K	Vapor-liquid equilibrium data of binary mixtures of 1-hexanol, 1-heptanol, 1-nonanol and 1,3-propanediol at P = 101.3 kPa using differential scanning calorimetry (DSC)
Tboil	430.44	K	ChemSep v8.3 pure component data Compiled value
Tboil	430.70	K	KDB
Tboil	430.15	K	NCMS SOLV-DB
Tboil	429.70	K	NIST
Tboil	431.20	K	NIST
Tboil	430.50	K	NIST
Tboil	430.00 ± 0.12	K	NIST
Tboil	430.50 ± 0.50	K	NIST
Tboil	430.40 ± 0.30	K	NIST
Tboil	430.25	K	NIST
Tboil	430.55 ± 0.50	K	NIST
Tboil	430.65 ± 0.70	K	NIST
Tboil	429.40 ± 0.70	K	NIST
Tboil	428.15 ± 1.00	K	NIST
Tboil	430.25	K	NIST
Tboil	428.15 ± 1.00	K	NIST
Tboil	427.65 ± 3.00	K	NIST
Tboil	430.15 ± 2.00	K	NIST
Tboil	429.65 ± 2.00	K	NIST
Tboil	431.15 ± 2.00	K	NIST
Tboil	426.65 ± 2.00	K	NIST
Tboil	430.55 ± 0.30	K	NIST
Tboil	426.90 ± 2.00	K	NIST
Tboil	430.45 ± 0.50	K	NIST
Tboil	428.65 ± 1.50	K	NIST
Tboil	430.27 ± 0.20	K	NIST
Tboil	429.65 ± 1.00	K	NIST
Tboil	430.95 ± 0.70	K	NIST
Tboil	429.65 ± 2.00	K	NIST
Tboil	425.65 ± 3.00	K	NIST
Tboil	429.75 ± 0.70	K	NIST
Tboil	430.15 ± 0.70	K	NIST
Tboil	428.90 ± 0.70	K	NIST
Tboil	429.90 ± 1.00	K	NIST
Tboil	428.65 ± 2.00	K	NIST
Tboil	430.65 ± 1.00	K	NIST
Tboil	431.05 ± 0.50	K	NIST
Tboil	428.65 ± 2.00	K	NIST
Tboil	428.45 ± 2.00	K	NIST
Tboil	429.60 ± 0.70	K	NIST
Tboil	430.55 ± 1.00	K	NIST
Tboil	430.62 ± 0.20	K	NIST
Tboil	428.85 ± 0.30	K	NIST
Tboil	Outlier 421.15 ± 2.00	K	NIST
Tboil	429.65 ± 0.50	K	NIST
Tboil	431.00 ± 0.30	K	NIST
Tboil	430.20 ± 0.50	K	NIST
Tboil	430.95 ± 0.50	K	NIST
Tboil	430.80 ± 0.30	K	NIST
Tboil	432.15 ± 2.00	K	NIST
Tboil	430.15 ± 0.70	K	NIST
Tboil	429.00 ± 0.40	K	NIST
Tboil	Outlier 440.15 ± 5.00	K	NIST
Tboil	431.15 ± 2.00	K	NIST
Tboil	Outlier 409.15 ± 3.00	K	NIST
Tboil	428.15 ± 2.00	K	NIST
Tboil	428.70 ± 0.70	K	NIST
Tboil	430.15 ± 3.00	K	NIST
Tboil	429.00 ± 3.00	K	NIST
Tboil	429.75 ± 1.00	K	NIST
Tboil	430.60 ± 1.00	K	NIST
Tboil	430.45 ± 2.00	K	NIST
Tboil	423.15 ± 4.00	K	NIST
Tc	[610.00; 611.40]	K
Tc	610.30	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Tc	610.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	611.40	K	ChemSep v8.3 pure component data Compiled value
Tc	610.30	K	KDB
Tc	610.30 ± 0.50	K	NIST
Tc	610.40 ± 0.80	K	NIST
Tc	610.40 ± 0.60	K	NIST
Tc	610.40 ± 0.60	K	NIST
Tc	611.00	K	NIST
Tc	611.35 ± 0.30	K	NIST
Tc	610.00	K	NIST
Tc	610.00 ± 2.00	K	NIST
Tfus	[221.20; 229.00]	K
Tfus	229.00	K	Vapour liquid equilibria, azeotropic data, excess enthalpies, activity coefficients at infinite dilution and solid liquid equilibria for binary alcohol ketone systems
Tfus	226.00	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	228.55	K	ChemSep v8.3 pure component data Compiled value
Tfus	228.50	K	KDB
Tfus	224.75	K	Aq. Solubility Prediction
Tfus	228.55	K	NCMS SOLV-DB
Tfus	228.55	K	NIST
Tfus	228.55	K	NIST
Tfus	226.45 ± 0.40	K	NIST
Tfus	Outlier 221.20 ± 0.50	K	NIST
Tfus	227.10 ± 0.50	K	NIST
Tfus	226.00 ± 2.00	K	NIST
Tfus	221.60 ± 0.50	K	NIST
Ttriple	[225.80; 228.55]	K
Ttriple	228.55	K	ChemSep v8.3 pure component data Compiled value
Ttriple	225.80 ± 0.30	K	NIST
Ttriple	225.80 ± 0.30	K	NIST
UQi	4.75		ChemSep v8.3 pure component data Compiled value
URi	5.27		ChemSep v8.3 pure component data Compiled value
Vc	[0.381; 0.387]	m3/kmol
Vc	0.387	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Vc	0.381	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.381	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.387	m3/kmol	KDB
Vc	0.387	m3/kmol	NIST
Zc	[0.2606010; 0.2630000]
Zc	0.2610000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Zc	0.2630000		ChemSep v8.3 pure component data Compiled value
Zc	0.2606010		KDB
Zra	0.26		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[232.46; 249.15]	J/mol×K	[290.01; 303.74]
Cp,liquid	232.46	J/mol×K	290.01	NIST
Cp,liquid	236.50	J/mol×K	293.15	NIST
Cp,liquid	236.50	J/mol×K	293.15	NIST
Cp,liquid	244.80	J/mol×K	298.00	NIST
Cp,liquid	239.62	J/mol×K	298.15	NIST
Cp,liquid	239.68	J/mol×K	298.15	NIST
Cp,liquid	243.20	J/mol×K	298.15	NIST
Cp,liquid	241.32	J/mol×K	298.15	NIST
Cp,liquid	240.65	J/mol×K	298.15	NIST
Cp,liquid	240.57	J/mol×K	298.15	NIST
Cp,liquid	237.85	J/mol×K	298.15	NIST
Cp,liquid	241.32	J/mol×K	298.15	NIST
Cp,liquid	242.50	J/mol×K	298.15	NIST
Cp,liquid	249.15	J/mol×K	300.61	NIST
Cp,liquid	247.70	J/mol×K	303.74	NIST
η	[0.0014110; 0.0074590]	Pa×s	[283.15; 343.15]
η	0.0074590	Pa×s	283.15	Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
η	0.0053350	Pa×s	293.15	Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
η	0.0054120	Pa×s	293.15	A Study on Properties Derived from Densities and Viscosities for the Ternary Systems (Methyl Pentanoate or Methyl Heptanoate) + n-Octane + 1-Hexanol and their Binary Subsystems at Various Temperatures.
η	0.0046426	Pa×s	298.15	Densities, Viscosities, and Volumetric Properties of Binary Mixtures of 1,2-Propanediol + 1-Heptanol or 1-Hexanol and 1,2-Ethanediol + 2-Butanol or 2-Propanol at T = (298.15, 303.15, and 308.15) K
η	0.0045960	Pa×s	298.15	A Study on Properties Derived from Densities and Viscosities for the Ternary Systems (Methyl Pentanoate or Methyl Heptanoate) + n-Octane + 1-Hexanol and their Binary Subsystems at Various Temperatures.
η	0.0045920	Pa×s	298.15	NCMS SOLV-DB
η	0.0045940	Pa×s	298.15	Acoustical and Excess Properties of {Chlorobenzene + 1-Hexanol, or 1-Heptanol, or 1-Octanol, or 1-Nonanol, or 1-Decanol} at (298.15, 303.15, 308.15, and 313.15) K
η	0.0046050	Pa×s	298.15	Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
η	0.0038870	Pa×s	303.15	Acoustical and Excess Properties of {Chlorobenzene + 1-Hexanol, or 1-Heptanol, or 1-Octanol, or 1-Nonanol, or 1-Decanol} at (298.15, 303.15, 308.15, and 313.15) K
η	0.0039985	Pa×s	303.15	Densities, Viscosities, and Volumetric Properties of Binary Mixtures of 1,2-Propanediol + 1-Heptanol or 1-Hexanol and 1,2-Ethanediol + 2-Butanol or 2-Propanol at T = (298.15, 303.15, and 308.15) K
η	0.0038290	Pa×s	303.15	Volumetric and Viscometric Behavior of the Binary System: (Hexan-1-ol + p-Xylene)
η	0.0038290	Pa×s	303.15	Thermodynamic Properties of the Binary Mixture of Hexan-1-ol with m-Xylene at T = (303.15, 313.15, and 323.15) K
η	0.0039440	Pa×s	303.15	Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
η	0.0039170	Pa×s	303.15	Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
η	0.0037630	Pa×s	303.15	Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
η	0.0039640	Pa×s	303.15	A Study on Properties Derived from Densities and Viscosities for the Ternary Systems (Methyl Pentanoate or Methyl Heptanoate) + n-Octane + 1-Hexanol and their Binary Subsystems at Various Temperatures.
η	0.0033180	Pa×s	308.15	Density and Viscosity of the Binary Mixtures of Hexan-1-ol with Isomeric Xylenes at T = (308.15 and 318.15) K and Atmospheric Pressure
η	0.0034713	Pa×s	308.15	Densities, Viscosities, and Volumetric Properties of Binary Mixtures of 1,2-Propanediol + 1-Heptanol or 1-Hexanol and 1,2-Ethanediol + 2-Butanol or 2-Propanol at T = (298.15, 303.15, and 308.15) K
η	0.0034140	Pa×s	308.15	Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
η	0.0033590	Pa×s	308.15	Acoustical and Excess Properties of {Chlorobenzene + 1-Hexanol, or 1-Heptanol, or 1-Octanol, or 1-Nonanol, or 1-Decanol} at (298.15, 303.15, 308.15, and 313.15) K
η	0.0029600	Pa×s	313.15	Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
η	0.0029370	Pa×s	313.15	Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
η	0.0029660	Pa×s	313.15	A Study on Properties Derived from Densities and Viscosities for the Ternary Systems (Methyl Pentanoate or Methyl Heptanoate) + n-Octane + 1-Hexanol and their Binary Subsystems at Various Temperatures.
η	0.0029140	Pa×s	313.15	Acoustical and Excess Properties of {Chlorobenzene + 1-Hexanol, or 1-Heptanol, or 1-Octanol, or 1-Nonanol, or 1-Decanol} at (298.15, 303.15, 308.15, and 313.15) K
η	0.0028790	Pa×s	313.15	Volumetric and Viscometric Behavior of the Binary System: (Hexan-1-ol + p-Xylene)
η	0.0028790	Pa×s	313.15	Thermodynamic Properties of the Binary Mixture of Hexan-1-ol with m-Xylene at T = (303.15, 313.15, and 323.15) K
η	0.0025180	Pa×s	318.15	Density and Viscosity of the Binary Mixtures of Hexan-1-ol with Isomeric Xylenes at T = (308.15 and 318.15) K and Atmospheric Pressure
η	0.0025810	Pa×s	318.15	Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
η	0.0022150	Pa×s	323.15	Thermodynamic Properties of the Binary Mixture of Hexan-1-ol with m-Xylene at T = (303.15, 313.15, and 323.15) K
η	0.0022510	Pa×s	323.15	Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
η	0.0022150	Pa×s	323.15	Volumetric and Viscometric Behavior of the Binary System: (Hexan-1-ol + p-Xylene)
η	0.0022760	Pa×s	323.15	Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
η	0.0021720	Pa×s	323.15	Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
η	0.0016540	Pa×s	333.15	Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
η	0.0014110	Pa×s	343.15	Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
εr	13.06		298.15	Comparative Dielectric Study and Molecular Interactions of Binary Mixtures of (Cyclohexanone + 1-Alkanols) and (Cyclopentanone or Cyclohexanone + Cyclohexanol or Cyclohexane) at T = 298.15 K
ΔfusH	[15.38; 15.48]	kJ/mol	[225.80; 225.80]
ΔfusH	15.38	kJ/mol	225.80	NIST
ΔfusH	15.48	kJ/mol	225.80	NIST
ΔfusH	15.48	kJ/mol	225.80	NIST
ΔvapH	[44.50; 62.00]	kJ/mol	[295.50; 430.50]
ΔvapH	61.20	kJ/mol	295.50	NIST
ΔvapH	62.00	kJ/mol	296.50	NIST
ΔvapH	61.90 ± 0.20	kJ/mol	300.50	NIST
ΔvapH	57.70	kJ/mol	320.50	NIST
ΔvapH	58.50 ± 0.20	kJ/mol	328.00	NIST
ΔvapH	57.60 ± 0.20	kJ/mol	343.00	NIST
ΔvapH	56.00	kJ/mol	357.50	NIST
ΔvapH	55.20 ± 0.20	kJ/mol	358.00	NIST
ΔvapH	59.70	kJ/mol	364.00	NIST
ΔvapH	53.80 ± 0.20	kJ/mol	368.00	NIST
ΔvapH	57.90	kJ/mol	369.00	NIST
ΔvapH	58.50	kJ/mol	378.00	NIST
ΔvapH	57.90	kJ/mol	379.00	NIST
ΔvapH	51.40	kJ/mol	393.00	NIST
ΔvapH	47.90	kJ/mol	398.50	NIST
ΔvapH	48.53	kJ/mol	430.30	KDB
ΔvapH	44.50	kJ/mol	430.50	NIST
ν	[0.0000036; 0.0000047]	m2/s	[303.15; 313.15]
ν	0.0000047	m2/s	303.15	Densities, Viscosities, and Ultrasonic Velocity Studies of Binary Mixtures of Chloroform with Pentan-1-ol, Hexan-1-ol, and Heptan-1-ol at (303.15 and 313.15) K
ν	0.0000036	m2/s	313.15	Densities, Viscosities, and Ultrasonic Velocity Studies of Binary Mixtures of Chloroform with Pentan-1-ol, Hexan-1-ol, and Heptan-1-ol at (303.15 and 313.15) K
Pvap	[1.43e-04; 106.98]	kPa	[237.95; 432.32]
Pvap	1.43e-04	kPa	237.95	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	1.43e-04	kPa	238.00	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	1.45e-04	kPa	238.00	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	2.96e-04	kPa	243.20	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	2.96e-04	kPa	243.20	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	2.93e-04	kPa	243.25	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	5.60e-04	kPa	248.20	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	5.64e-04	kPa	248.20	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	5.69e-04	kPa	248.20	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	1.06e-03	kPa	253.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	1.05e-03	kPa	253.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	1.05e-03	kPa	253.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	1.92e-03	kPa	258.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	1.92e-03	kPa	258.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	1.92e-03	kPa	258.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	3.39e-03	kPa	263.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	3.39e-03	kPa	263.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	3.38e-03	kPa	263.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	4.68e-03	kPa	265.00	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	5.84e-03	kPa	268.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	5.84e-03	kPa	268.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	5.84e-03	kPa	268.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	6.64e-03	kPa	268.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	9.87e-03	kPa	273.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	9.86e-03	kPa	273.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	9.87e-03	kPa	273.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	0.01	kPa	273.40	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.01	kPa	273.65	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	0.01	kPa	273.65	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	0.01	kPa	273.65	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	0.02	kPa	278.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	0.02	kPa	278.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	0.02	kPa	278.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	0.02	kPa	278.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.03	kPa	283.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	0.03	kPa	283.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	0.03	kPa	283.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	0.03	kPa	283.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.05	kPa	288.10	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.04	kPa	288.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	0.04	kPa	288.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	0.04	kPa	288.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	0.07	kPa	293.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	0.07	kPa	293.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	0.07	kPa	293.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	0.07	kPa	293.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.07	kPa	293.30	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.10	kPa	298.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	0.12	kPa	298.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	0.11	kPa	298.15	NCMS SOLV-DB
Pvap	0.10	kPa	298.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	0.10	kPa	298.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	0.12	kPa	298.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.11	kPa	298.30	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.15	kPa	303.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	0.15	kPa	303.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	0.17	kPa	303.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	0.15	kPa	303.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	0.17	kPa	303.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.17	kPa	303.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.17	kPa	303.30	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.22	kPa	308.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	0.22	kPa	308.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	0.22	kPa	308.15	Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap	0.25	kPa	308.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	0.25	kPa	308.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.25	kPa	308.30	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.30	kPa	310.40	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.36	kPa	313.10	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.36	kPa	313.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	0.37	kPa	313.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.52	kPa	318.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	0.53	kPa	318.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.53	kPa	318.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.73	kPa	323.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	0.71	kPa	323.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.75	kPa	323.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	1.03	kPa	328.10	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	1.01	kPa	328.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	1.01	kPa	328.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	1.43	kPa	333.10	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	1.40	kPa	333.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	1.46	kPa	333.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	1.90	kPa	338.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	1.98	kPa	338.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	2.54	kPa	343.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	2.64	kPa	343.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	2.04	kPa	343.46	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	2.16	kPa	344.20	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	2.23	kPa	344.60	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	2.35	kPa	345.36	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	2.47	kPa	346.17	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	2.67	kPa	347.27	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	2.79	kPa	348.10	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	3.38	kPa	348.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	3.48	kPa	348.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	2.85	kPa	348.35	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	3.04	kPa	349.38	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	3.11	kPa	349.75	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	3.32	kPa	350.75	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	3.44	kPa	351.39	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	3.64	kPa	352.20	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	3.73	kPa	352.63	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	3.83	kPa	353.00	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	4.43	kPa	353.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	4.64	kPa	353.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	3.89	kPa	353.31	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	3.96	kPa	353.82	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	4.31	kPa	355.20	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	4.79	kPa	357.01	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	5.79	kPa	357.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	5.76	kPa	358.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	6.13	kPa	358.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	5.15	kPa	358.22	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	5.51	kPa	359.43	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	5.79	kPa	360.34	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	6.04	kPa	361.12	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	6.29	kPa	361.86	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	7.41	kPa	363.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	7.87	kPa	363.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	6.99	kPa	363.85	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	7.27	kPa	364.61	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	7.64	kPa	365.58	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	7.92	kPa	366.30	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	8.32	kPa	366.67	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	8.40	kPa	367.44	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	8.67	kPa	368.05	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	9.44	kPa	368.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	9.08	kPa	368.99	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	9.40	kPa	369.67	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	9.67	kPa	370.24	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	9.95	kPa	370.83	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	10.27	kPa	371.45	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	10.59	kPa	372.10	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	11.06	kPa	372.64	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	11.05	kPa	373.00	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	11.91	kPa	373.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	11.43	kPa	373.67	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	11.73	kPa	374.19	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	12.27	kPa	375.14	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	12.73	kPa	375.93	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	13.15	kPa	376.59	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	13.53	kPa	377.22	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	13.87	kPa	377.56	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	13.71	kPa	377.83	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	13.85	kPa	378.01	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	14.90	kPa	378.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	14.15	kPa	378.37	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	14.40	kPa	378.72	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	14.65	kPa	379.10	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	14.91	kPa	379.46	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	15.12	kPa	379.75	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	15.37	kPa	380.06	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	15.61	kPa	380.41	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	15.95	kPa	380.87	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	16.15	kPa	381.15	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	16.37	kPa	381.45	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	16.77	kPa	381.80	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	16.77	kPa	381.81	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	16.71	kPa	381.89	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	16.97	kPa	382.25	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	17.21	kPa	382.56	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	17.44	kPa	382.85	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	18.50	kPa	383.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	17.69	kPa	383.18	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	17.84	kPa	383.34	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	18.09	kPa	383.67	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	18.43	kPa	384.08	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	19.05	kPa	384.87	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	19.47	kPa	385.37	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	19.91	kPa	385.86	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	20.26	kPa	386.17	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	20.31	kPa	386.31	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	20.79	kPa	386.83	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	21.15	kPa	387.23	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	21.48	kPa	387.62	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	21.91	kPa	388.10	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	22.79	kPa	388.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	22.37	kPa	388.59	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	22.79	kPa	389.05	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	23.20	kPa	389.48	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	23.60	kPa	389.89	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	23.95	kPa	390.23	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	24.36	kPa	390.65	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	24.54	kPa	390.77	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	24.54	kPa	390.78	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	24.67	kPa	390.93	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	25.00	kPa	391.07	Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap	25.13	kPa	391.40	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	25.51	kPa	391.75	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	25.83	kPa	392.06	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	26.31	kPa	392.51	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	26.59	kPa	392.77	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	27.00	kPa	393.14	Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap	27.86	kPa	393.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	29.35	kPa	395.23	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	29.35	kPa	395.23	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	30.00	kPa	395.62	Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap	33.84	kPa	398.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	34.77	kPa	399.57	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	35.00	kPa	399.65	Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap	40.00	kPa	402.36	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	40.00	kPa	403.15	Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap	40.85	kPa	403.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	40.02	kPa	403.66	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	40.70	kPa	403.73	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	45.00	kPa	406.36	Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap	48.72	kPa	407.89	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	47.57	kPa	407.98	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	49.02	kPa	408.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	50.00	kPa	409.25	Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap	55.00	kPa	411.92	Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap	58.50	kPa	413.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	58.84	kPa	413.31	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	60.00	kPa	414.44	Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap	60.20	kPa	414.61	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	65.00	kPa	416.75	Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap	69.49	kPa	418.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	69.27	kPa	418.35	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	70.00	kPa	418.98	Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap	74.69	kPa	420.99	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	75.00	kPa	421.05	Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap	77.40	kPa	421.90	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	80.00	kPa	423.01	Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap	82.16	kPa	423.15	Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap	85.00	kPa	424.87	Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap	85.63	kPa	425.15	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	90.00	kPa	426.69	Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap	92.07	kPa	427.54	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	93.19	kPa	427.85	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	93.26	kPa	427.90	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	99.78	kPa	429.19	Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap	98.12	kPa	429.52	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	98.16	kPa	429.54	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	101.30	kPa	430.11	Vapor-liquid equilibrium data of binary mixtures of 1-hexanol, 1-heptanol, 1-nonanol and 1,3-propanediol at P = 101.3 kPa using differential scanning calorimetry (DSC)
Pvap	105.46	kPa	431.85	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	106.75	kPa	432.25	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap	106.98	kPa	432.32	Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
n0	[1.41270; 1.42070]		[293.10; 313.15]
n0	1.41800		293.10	Viscosity and surface tension of binary systems of N,N-dimethylformamide with alkan-1-ols at different temperatures
n0	1.41750		293.15	Measurement and Correlation of the Solubilities of m-Phthalic Acid in Monobasic Alcohols
n0	1.41830		293.15	Densities, Excess Molar Volumes, and Isobaric Thermal Expansibilities for 1,2-Ethanediol + 1-Butanol, or 1-Hexanol, or 1-Octanol in the Temperature Range from (293.15 to 313.15) K
n0	1.41826		293.15	Excess molar volumes and viscosities of (1,1,2,2-tetrabromoethane + 1-alkanols) at T = (293.15 and 303.15) K
n0	1.41807		293.15	Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrachloroethane and 1-alkanols binary mixtures
n0	1.41780		293.15	Densities, Viscosities, Speeds of Sound, and Refractive Indices for Binary Mixtures of Diethylcarbonate, Acetophenone, and 1-Hexanol at (293.15, 303.15, 313.15, and 323.15) K for the Liquid Region and at Ambient Pressure
n0	1.41826		293.15	Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrabromoethane and 1-alkanols binary mixtures
n0	1.41780		293.15	Densities and derived thermodynamic properties of binary mixtures of diethylcarbonate, acetophenone, and 1-hexanol at T = (293.15 to 323.15) K for the liquid region and at ambient pressure
n0	1.41800		293.15	ERAS modeling of the excess molar enthalpies of binary liquid mixtures of 1-pentanol and 1-hexanol with acetonitrile at atmospheric pressure and 288, 298, 313 and 323K
n0	1.41810		293.20	Liquid-liquid equilibrium data for systems containing of formic acid, water, and primary normal alcohols at T = 298.2 K
n0	1.42070		293.20	Vapor Liquid Equilibrium Data for Binary Systems of 1-Methyl-4-(1-methylethenyl)-cyclohexene + {Ethanol, Propan-1-ol, Propan-2-ol, Butan-1-ol, Pentan-1-ol, or Hexan-1-ol} at 40 kPa
n0	1.41580		298.15	Liquid Liquid Phase Equilibria of 1-Propanol + Water + n-Alcohol Ternary Systems at 298.15 K and Atmospheric Pressure
n0	1.41570		298.15	Effect of Pressure on the Static Relative Permittivities of Alkan-1-ols at 298.15 K
n0	1.41600		298.15	NCMS SOLV-DB
n0	1.41570		298.15	Vapor-Liquid Equilibria of Binary Mixtures Formed by Hexan-1-ol with Chloroethanes and Chloroethenes at 95.6 kPa
n0	1.41620		298.15	Phase equilibria in the ternary system isobutyl alcohol + isobutyl acetate + 1-hexanol and the binary systems isobutyl alcohol + 1-hexanol, isobutyl acetate + 1-hexanol at 101.3 kPa
n0	1.41550		298.15	Ternary liquid liquid equilibrium data for the (water + butyric acid + n-hexane or n-hexanol) systems at T = (298.2, 308.2, and 318.2) K
n0	1.41600		298.15	Liquid-liquid equilibrium for (water + 5-hydroxymethylfurfural + 1-pentanol/1-hexanol/1-heptanol) systems at 298.15 K
n0	1.41600		298.15	Comparative study of physico-chemical properties of binary mixtures of N,N-dimethylformamide with 1-alkanols at different temperatures
n0	1.41610		298.15	Permittivities, Refractive Indices, Densities, and Excess Properties for Binary Systems Containing 1-Alkanols and Cyclopentanone
n0	1.41590		298.15	Density, Surface Tension, and Refractive Index of Octane + 1-Alkanol Mixtures at T ) 298.15 K.
n0	1.41660		298.15	Excess Molar Enthalpies of 1,2-Propanediol + Alkan-1-ols (C1-C6) and Their Correlations at 298.15 K and Ambient Pressure (81.5 kPa)
n0	1.41610		298.15	Densities, Excess Molar Volumes, and Isobaric Thermal Expansibilities for 1,2-Ethanediol + 1-Butanol, or 1-Hexanol, or 1-Octanol in the Temperature Range from (293.15 to 313.15) K
n0	1.41650		298.15	Excess Molar Enthalpies of Benzyl Alcohol + Alkanols (C1-C6) and Their Correlations at 298.15 K and Ambient Pressure
n0	1.41738		298.15	Atmospheric densities and interfacial tensions for 1- alkanol (1-butanol to 1-octanol) + water and ether (MTBE, ETBE, DIPE, TAME and THP) + water demixed mixtures.
n0	1.41550		298.20	Ternary equilibrium data of mixtures consisting of 2-butanol, water, and heavy alcohols at T = 298.2 K
n0	1.41423		303.15	Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrabromoethane and 1-alkanols binary mixtures
n0	1.41423		303.15	Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrachloroethane and 1-alkanols binary mixtures
n0	1.41340		303.15	Measurements of the Properties of Binary Mixtures of Dimethylsulphoxide (DMSO) with 1-Alkanols (C4, C6, C7) at 303.15K
n0	1.41570		303.15	Comparative study of physico-chemical properties of binary mixtures of N,N-dimethylformamide with 1-alkanols at different temperatures
n0	1.41410		308.15	Comparative study of physico-chemical properties of binary mixtures of N,N-dimethylformamide with 1-alkanols at different temperatures
n0	1.41270		313.15	Comparative study of physico-chemical properties of binary mixtures of N,N-dimethylformamide with 1-alkanols at different temperatures
ρl	[765.64; 827.82]	kg/m3	[283.15; 363.15]
ρl	825.94	kg/m3	283.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl	827.82	kg/m3	283.15	Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
ρl	826.03	kg/m3	283.15	Excess molar volumes of binary mixtures of 1,3-dimethylimidazolidin-2-one with an alkan-1-ol at the temperatures 283.15 K, 298.15 K, and 313.15 K
ρl	824.25	kg/m3	288.15	Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
ρl	822.00	kg/m3	288.15	Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl	822.26	kg/m3	288.15	Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl	822.26	kg/m3	288.15	Volumetric and transport properties of binary liquid mixtures with 1-ethyl-3-methylimidazolium ethyl sulfate as candidate solvents for regenerative flue gas desulfurization processes
ρl	822.42	kg/m3	288.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl	819.00	kg/m3	293.00	KDB
ρl	818.90	kg/m3	293.15	Density and Viscosity of Binary Liquid Mixtures of Ethanol + 1-Hexanol and Ethanol + 1-Heptanol from (293.15 to 328.15) K at 0.1 MPa
ρl	818.00	kg/m3	293.15	Densities, Viscosities, and Refractive Indices of Dimethyl Carbonate + 1-Hexanol/1-Octanol Binary Mixtures at Different Temperatures
ρl	818.70	kg/m3	293.15	Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl	819.00	kg/m3	293.15	Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl	818.69	kg/m3	293.15	Volumetric and transport properties of binary liquid mixtures with 1-ethyl-3-methylimidazolium ethyl sulfate as candidate solvents for regenerative flue gas desulfurization processes
ρl	818.88	kg/m3	293.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl	818.70	kg/m3	293.15	Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl	818.70	kg/m3	293.15	Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl	818.75	kg/m3	293.15	Volume effects for binary mixtures of propane-1,2-diol with methanol, propan-1-ol, hexan-1-ol, octan-1-ol, or nonan-1-ol at temperatures (293.15 to 318.15) K
ρl	820.65	kg/m3	293.15	Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
ρl	815.16	kg/m3	298.10	Excess Molar Enthalpies of Propyl Propanoate + 1-Hexanol + Benzene at the Temperatures of 25 :C and 35 :C
ρl	815.30	kg/m3	298.15	Bubble point measurements of binary mixtures formed by 1-hexanol with selected nitro-compounds and substituted benzenes at 95.6 kPa
ρl	815.65	kg/m3	298.15	Thermodynamic, transport and excess properties of 2-butoxy ethanol +1-alkanol (C6,C8,C10) at different temperatures
ρl	815.21	kg/m3	298.15	Excess molar enthalpies of binary systems containing 2-octanone, hexanoic acid, or octanoic acid at T = 298.15 K
ρl	815.20	kg/m3	298.15	Effect of temperature and composition on the density, viscosity, surface tension, and thermodynamic properties of binary mixtures of N-octylisoquinolinium bis{(trifluoromethyl)sulfonyl}imide with alcohols
ρl	815.27	kg/m3	298.15	Density and Relative Permittivity for 1-Alkanols + Dodecane at 298.15 K
ρl	815.34	kg/m3	298.15	Excess molar volumes of binary mixtures of 1,3-dimethylimidazolidin-2-one with an alkan-1-ol at the temperatures 283.15 K, 298.15 K, and 313.15 K
ρl	815.50	kg/m3	298.15	Viscosities and Densities of Fatty Alcohol Mixtures from 298.15 to 338.15 K: Estimation by Kay's Rule and Prediction by the UNIFAC-VISCO and GC-UNIMOD Group Contribution Methods
ρl	815.15	kg/m3	298.15	Speeds of Sound and Isentropic Compressibilities in Binary Mixtures of 2-Propanol with Several 1-Alkanols at 298.15K
ρl	815.26	kg/m3	298.15	Studies of thermophysical properties of binary liquid mixtures of amine and alcohols at various temperatures
ρl	815.20	kg/m3	298.15	Excess molar enthalpies of methyl isobutyl ketone (MIBK) with alkan-1-ols (C1-C6) and their correlations at 298.15 K
ρl	815.19	kg/m3	298.15	Volume effects for binary mixtures of propane-1,2-diol with methanol, propan-1-ol, hexan-1-ol, octan-1-ol, or nonan-1-ol at temperatures (293.15 to 318.15) K
ρl	815.10	kg/m3	298.15	Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl	814.94	kg/m3	298.15	Phase behaviour of tricyanomethanide-based ionic liquids with alcohols and hydrocarbons
ρl	815.10	kg/m3	298.15	Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl	815.11	kg/m3	298.15	Volumetric and transport properties of binary liquid mixtures with 1-ethyl-3-methylimidazolium ethyl sulfate as candidate solvents for regenerative flue gas desulfurization processes
ρl	815.30	kg/m3	298.15	Bubble point measurements of binary mixtures formed by ethyl benzene with selected compounds at 95.35 kPa
ρl	815.31	kg/m3	298.15	FT-IR studies on excess thermodynamic properties of binary liquid mixtures o-chlorotoluene with 1-propanol, 1-butanol, 1-pentanol, 1-hexanol and 1-heptanol at different temperatures
ρl	815.32	kg/m3	298.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl	814.94	kg/m3	298.15	Phase behaviour of ionic liquid 1-butyl-1-methylpyrrolidinium tris(pentafluoroethyl)trifluorophosphate with alcohols, water and aromatic hydrocarbons
ρl	815.29	kg/m3	298.15	Densities, speeds of sound and viscosities of binary mixtures of tetrahydrofuran with 1-hexanol, 1-octanol and 1-decanol at T = (298.15 to 313.15) K
ρl	815.90	kg/m3	298.15	Excess volumes and partial molar volumes of binary liquid mixtures of furfural or 2-methylfuran with alcohols at 298.15 K
ρl	815.40	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
ρl	815.00	kg/m3	298.15	Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl	815.12	kg/m3	298.15	Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl	815.30	kg/m3	298.15	Density and Viscosity of Binary Liquid Mixtures of Ethanol + 1-Hexanol and Ethanol + 1-Heptanol from (293.15 to 328.15) K at 0.1 MPa
ρl	815.70	kg/m3	298.15	Thermodynamics of 1,3-dimethylurea in eight alcohols
ρl	814.90	kg/m3	298.15	Densities, Viscosities, and Refractive Indices of Dimethyl Carbonate + 1-Hexanol/1-Octanol Binary Mixtures at Different Temperatures
ρl	814.95	kg/m3	298.15	Densities and Excess Molar Volumes of N-Methylmorpholine + 1-Alkanol Systems at 298.15 K
ρl	815.02	kg/m3	298.15	Surface Properties of Binary Mixtures of Ethylene Glycol with a Series of Aliphatic Alcohols (1-Pentanol, 1-Hexanol, and 1-Heptanol)
ρl	817.03	kg/m3	298.15	Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
ρl	815.17	kg/m3	298.20	Liquid-liquid equilibrium data for ternary systems of water + lactic acid + C4-C7 alcohols at 298.2 K and atmospheric pressure
ρl	815.88	kg/m3	298.20	Isothermal vapor-liquid equilibria, excess molar volume and the deviation of refractive indices for binary mixtures of 1-butanol, 1- hexanol, 3-methyl-1-butanol and butyl acetate
ρl	811.50	kg/m3	303.15	Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl	812.00	kg/m3	303.15	Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl	813.39	kg/m3	303.15	Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
ρl	811.70	kg/m3	303.15	Density and Viscosity of Binary Liquid Mixtures of Ethanol + 1-Hexanol and Ethanol + 1-Heptanol from (293.15 to 328.15) K at 0.1 MPa
ρl	811.52	kg/m3	303.15	Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl	811.51	kg/m3	303.15	Volumetric and transport properties of binary liquid mixtures with 1-ethyl-3-methylimidazolium ethyl sulfate as candidate solvents for regenerative flue gas desulfurization processes
ρl	811.39	kg/m3	303.15	Excess molar enthalpies and heat capacities of dimethyl sulfoxide + seven normal alkanols at 303.15K and atmospheric pressure
ρl	811.60	kg/m3	303.15	Volume effects for binary mixtures of propane-1,2-diol with methanol, propan-1-ol, hexan-1-ol, octan-1-ol, or nonan-1-ol at temperatures (293.15 to 318.15) K
ρl	811.50	kg/m3	303.15	Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl	811.30	kg/m3	303.15	Densities, Viscosities, and Refractive Indices of Dimethyl Carbonate + 1-Hexanol/1-Octanol Binary Mixtures at Different Temperatures
ρl	811.74	kg/m3	303.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl	811.70	kg/m3	303.15	FT-IR studies on excess thermodynamic properties of binary liquid mixtures o-chlorotoluene with 1-propanol, 1-butanol, 1-pentanol, 1-hexanol and 1-heptanol at different temperatures
ρl	807.90	kg/m3	308.15	Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl	808.00	kg/m3	308.15	Effect of temperature and composition on the density, viscosity, surface tension, and thermodynamic properties of binary mixtures of N-octylisoquinolinium bis{(trifluoromethyl)sulfonyl}imide with alcohols
ρl	807.98	kg/m3	308.15	Volume effects for binary mixtures of propane-1,2-diol with methanol, propan-1-ol, hexan-1-ol, octan-1-ol, or nonan-1-ol at temperatures (293.15 to 318.15) K
ρl	807.90	kg/m3	308.15	Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl	807.89	kg/m3	308.15	Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl	808.06	kg/m3	308.15	FT-IR studies on excess thermodynamic properties of binary liquid mixtures o-chlorotoluene with 1-propanol, 1-butanol, 1-pentanol, 1-hexanol and 1-heptanol at different temperatures
ρl	809.71	kg/m3	308.15	Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
ρl	807.60	kg/m3	308.15	Densities, Viscosities, and Refractive Indices of Dimethyl Carbonate + 1-Hexanol/1-Octanol Binary Mixtures at Different Temperatures
ρl	808.13	kg/m3	308.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl	808.40	kg/m3	308.15	Viscosities and Densities of Fatty Alcohol Mixtures from 298.15 to 338.15 K: Estimation by Kay's Rule and Prediction by the UNIFAC-VISCO and GC-UNIMOD Group Contribution Methods
ρl	807.88	kg/m3	308.15	Volumetric and transport properties of binary liquid mixtures with 1-ethyl-3-methylimidazolium ethyl sulfate as candidate solvents for regenerative flue gas desulfurization processes
ρl	808.10	kg/m3	308.15	Density and Viscosity of Binary Liquid Mixtures of Ethanol + 1-Hexanol and Ethanol + 1-Heptanol from (293.15 to 328.15) K at 0.1 MPa
ρl	804.46	kg/m3	313.15	Excess molar volumes of binary mixtures of 1,3-dimethylimidazolidin-2-one with an alkan-1-ol at the temperatures 283.15 K, 298.15 K, and 313.15 K
ρl	804.23	kg/m3	313.15	Volumetric and transport properties of binary liquid mixtures with 1-ethyl-3-methylimidazolium ethyl sulfate as candidate solvents for regenerative flue gas desulfurization processes
ρl	804.50	kg/m3	313.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl	803.90	kg/m3	313.15	Densities, Viscosities, and Refractive Indices of Dimethyl Carbonate + 1-Hexanol/1-Octanol Binary Mixtures at Different Temperatures
ρl	806.00	kg/m3	313.15	Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
ρl	804.20	kg/m3	313.15	Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl	805.00	kg/m3	313.15	Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl	804.50	kg/m3	313.15	Density and Viscosity of Binary Liquid Mixtures of Ethanol + 1-Hexanol and Ethanol + 1-Heptanol from (293.15 to 328.15) K at 0.1 MPa
ρl	804.25	kg/m3	313.15	Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl	804.34	kg/m3	313.15	Volume effects for binary mixtures of propane-1,2-diol with methanol, propan-1-ol, hexan-1-ol, octan-1-ol, or nonan-1-ol at temperatures (293.15 to 318.15) K
ρl	804.20	kg/m3	313.15	Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl	801.00	kg/m3	318.15	Viscosities and Densities of Fatty Alcohol Mixtures from 298.15 to 338.15 K: Estimation by Kay's Rule and Prediction by the UNIFAC-VISCO and GC-UNIMOD Group Contribution Methods
ρl	800.56	kg/m3	318.15	Volumetric and transport properties of binary liquid mixtures with 1-ethyl-3-methylimidazolium ethyl sulfate as candidate solvents for regenerative flue gas desulfurization processes
ρl	800.60	kg/m3	318.15	Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl	802.27	kg/m3	318.15	Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
ρl	800.66	kg/m3	318.15	Volume effects for binary mixtures of propane-1,2-diol with methanol, propan-1-ol, hexan-1-ol, octan-1-ol, or nonan-1-ol at temperatures (293.15 to 318.15) K
ρl	800.80	kg/m3	318.15	Density and Viscosity of Binary Liquid Mixtures of Ethanol + 1-Hexanol and Ethanol + 1-Heptanol from (293.15 to 328.15) K at 0.1 MPa
ρl	800.56	kg/m3	318.15	Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl	800.10	kg/m3	318.15	Densities, Viscosities, and Refractive Indices of Dimethyl Carbonate + 1-Hexanol/1-Octanol Binary Mixtures at Different Temperatures
ρl	800.83	kg/m3	318.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl	800.60	kg/m3	318.15	Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl	800.60	kg/m3	318.15	Effect of temperature and composition on the density, viscosity, surface tension, and thermodynamic properties of binary mixtures of N-octylisoquinolinium bis{(trifluoromethyl)sulfonyl}imide with alcohols
ρl	796.85	kg/m3	323.15	Volumetric and transport properties of binary liquid mixtures with 1-ethyl-3-methylimidazolium ethyl sulfate as candidate solvents for regenerative flue gas desulfurization processes
ρl	796.20	kg/m3	323.15	Densities, Viscosities, and Refractive Indices of Dimethyl Carbonate + 1-Hexanol/1-Octanol Binary Mixtures at Different Temperatures
ρl	796.80	kg/m3	323.15	Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl	798.49	kg/m3	323.15	Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
ρl	796.85	kg/m3	323.15	Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl	796.80	kg/m3	323.15	Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl	798.00	kg/m3	323.15	Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl	797.12	kg/m3	323.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl	797.10	kg/m3	323.15	Density and Viscosity of Binary Liquid Mixtures of Ethanol + 1-Hexanol and Ethanol + 1-Heptanol from (293.15 to 328.15) K at 0.1 MPa
ρl	794.67	kg/m3	328.15	Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
ρl	793.40	kg/m3	328.15	Density and Viscosity of Binary Liquid Mixtures of Ethanol + 1-Hexanol and Ethanol + 1-Heptanol from (293.15 to 328.15) K at 0.1 MPa
ρl	793.37	kg/m3	328.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl	793.20	kg/m3	328.15	Effect of temperature and composition on the density, viscosity, surface tension, and thermodynamic properties of binary mixtures of N-octylisoquinolinium bis{(trifluoromethyl)sulfonyl}imide with alcohols
ρl	793.50	kg/m3	328.15	Viscosities and Densities of Fatty Alcohol Mixtures from 298.15 to 338.15 K: Estimation by Kay's Rule and Prediction by the UNIFAC-VISCO and GC-UNIMOD Group Contribution Methods
ρl	790.80	kg/m3	333.15	Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
ρl	789.57	kg/m3	333.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl	791.00	kg/m3	333.15	Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl	785.50	kg/m3	338.15	Effect of temperature and composition on the density, viscosity, surface tension, and thermodynamic properties of binary mixtures of N-octylisoquinolinium bis{(trifluoromethyl)sulfonyl}imide with alcohols
ρl	785.90	kg/m3	338.15	Viscosities and Densities of Fatty Alcohol Mixtures from 298.15 to 338.15 K: Estimation by Kay's Rule and Prediction by the UNIFAC-VISCO and GC-UNIMOD Group Contribution Methods
ρl	785.72	kg/m3	338.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl	783.00	kg/m3	343.15	Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl	781.83	kg/m3	343.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl	777.86	kg/m3	348.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl	773.86	kg/m3	353.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl	769.78	kg/m3	358.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl	765.64	kg/m3	363.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ΔfusS	68.11	J/mol×K	225.80	NIST
csound,fluid	[1237.50; 1339.20]	m/s	[288.15; 318.15]
csound,fluid	1339.20	m/s	288.15	Ultrasonic study of molecular interactions in binary mixtures of methyl acrylate with 1-alkanols (C4 to C10) at temperatures from (288.15 to 318.15) K
csound,fluid	1320.38	m/s	293.15	Thermodynamic and spectral studies of molecular interactions in binary liquid mixtures of 1-butoxy-2- propanol with 1-alcohols
csound,fluid	1321.20	m/s	293.15	Ultrasonic study of molecular interactions in binary mixtures of methyl acrylate with 1-alkanols (C4 to C10) at temperatures from (288.15 to 318.15) K
csound,fluid	1320.32	m/s	293.15	Densities, Excess Molar Volumes, Speeds of Sound at (293.15, 298.15, and 303.15) K and Isentropic Compressibilities at 298.15 K for 1-Butanol, 1-Pentanol, or 1-Hexanol + Dibutylether Systems
csound,fluid	1320.11	m/s	293.15	Densities, Excess Molar Volumes, Ultrasonic Speeds, and Isentropic Compressibilities of Hexan-1-ol with 1,2-Dichloroethane, 1,2-Dibromoethane, and 1,1,2,2-Tetrachloroethene at (293.15 and 298.15) K
csound,fluid	1303.19	m/s	298.15	Densities, Excess Molar Volumes, Ultrasonic Speeds, and Isentropic Compressibilities of Hexan-1-ol with 1,2-Dichloroethane, 1,2-Dibromoethane, and 1,1,2,2-Tetrachloroethene at (293.15 and 298.15) K
csound,fluid	1312.40	m/s	298.15	Ultrasonic speeds and isentropic compressibilities of {difurylmethane + (C1 C6) n-alkanol} binary mixtures at T = 298.15 K
csound,fluid	1306.90	m/s	298.15	Ultrasonic study of molecular interactions in binary mixtures of methyl acrylate with 1-alkanols (C4 to C10) at temperatures from (288.15 to 318.15) K
csound,fluid	1303.03	m/s	298.15	Densities, Excess Molar Volumes, Speeds of Sound at (293.15, 298.15, and 303.15) K and Isentropic Compressibilities at 298.15 K for 1-Butanol, 1-Pentanol, or 1-Hexanol + Dibutylether Systems
csound,fluid	1303.54	m/s	298.15	Thermodynamic and spectral studies of molecular interactions in binary liquid mixtures of 1-butoxy-2- propanol with 1-alcohols
csound,fluid	1286.68	m/s	303.15	Thermodynamic and spectral studies of molecular interactions in binary liquid mixtures of 1-butoxy-2- propanol with 1-alcohols
csound,fluid	1289.50	m/s	303.15	Ultrasonic study of molecular interactions in binary mixtures of methyl acrylate with 1-alkanols (C4 to C10) at temperatures from (288.15 to 318.15) K
csound,fluid	1286.34	m/s	303.15	Densities, Excess Molar Volumes, Speeds of Sound at (293.15, 298.15, and 303.15) K and Isentropic Compressibilities at 298.15 K for 1-Butanol, 1-Pentanol, or 1-Hexanol + Dibutylether Systems
csound,fluid	1270.00	m/s	308.15	Thermodynamic and spectral studies of molecular interactions in binary liquid mixtures of 1-butoxy-2- propanol with 1-alcohols
csound,fluid	1275.70	m/s	308.15	Ultrasonic study of molecular interactions in binary mixtures of methyl acrylate with 1-alkanols (C4 to C10) at temperatures from (288.15 to 318.15) K
csound,fluid	1256.30	m/s	313.15	Ultrasonic study of molecular interactions in binary mixtures of methyl acrylate with 1-alkanols (C4 to C10) at temperatures from (288.15 to 318.15) K
csound,fluid	1253.54	m/s	313.15	Thermodynamic and spectral studies of molecular interactions in binary liquid mixtures of 1-butoxy-2- propanol with 1-alcohols
csound,fluid	1237.50	m/s	318.15	Ultrasonic study of molecular interactions in binary mixtures of methyl acrylate with 1-alkanols (C4 to C10) at temperatures from (288.15 to 318.15) K
γ	[0.02; 0.03]	N/m	[288.15; 328.15]
γ	0.03	N/m	288.15	The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ	0.03	N/m	288.15	Density and Surface Tension Variation with Temperature for Heptane + 1-Alkanol
γ	0.03	N/m	288.15	Study of surface tension and surface properties of binary systems of DMSO with long chain alcohols at various temperatures
γ	0.03	N/m	288.15	Density and surface tension variation with temperature for n-nonane + 1-hexanol
γ	0.03	N/m	293.15	Density and Surface Tension Variation with Temperature for Heptane + 1-Alkanol
γ	0.03	N/m	293.15	The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ	0.03	N/m	298.15	Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ	0.02	N/m	298.15	Study of surface tension and surface properties of binary systems of DMSO with long chain alcohols at various temperatures
γ	0.03	N/m	298.15	NCMS SOLV-DB
γ	0.03	N/m	298.15	Density and surface tension variation with temperature for n-nonane + 1-hexanol
γ	0.03	N/m	298.15	The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ	0.03	N/m	298.15	Density and Surface Tension Variation with Temperature for Heptane + 1-Alkanol
γ	0.03	N/m	298.20	KDB
γ	0.03	N/m	303.15	The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ	0.02	N/m	303.15	Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ	0.02	N/m	303.15	Density and Surface Tension Variation with Temperature for Heptane + 1-Alkanol
γ	0.02	N/m	308.15	The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ	0.02	N/m	308.15	Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ	0.02	N/m	308.15	Density and Surface Tension Variation with Temperature for Heptane + 1-Alkanol
γ	0.02	N/m	308.15	Density and surface tension variation with temperature for n-nonane + 1-hexanol
γ	0.02	N/m	308.15	Study of surface tension and surface properties of binary systems of DMSO with long chain alcohols at various temperatures
γ	0.02	N/m	313.15	The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ	0.02	N/m	313.15	Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ	0.02	N/m	318.15	The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ	0.02	N/m	318.15	Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ	0.02	N/m	318.15	Study of surface tension and surface properties of binary systems of DMSO with long chain alcohols at various temperatures
γ	0.02	N/m	323.15	Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ	0.02	N/m	328.15	Study of surface tension and surface properties of binary systems of DMSO with long chain alcohols at various temperatures

Datasets

1. Isobaric coefficient of expansion, 1/K (2)
2. Mass density, kg/m3 (8)
3. Speed of sound, m/s (1)

Isobaric coefficient of expansion, 1/K

Fixed		Measured
Pressure, kPa - Gas	Temperature, K - Gas	Isobaric coefficient of expansion, 1/K - Gas
5000.00	278.15	0.0008
5000.00	298.15	0.0009
5000.00	328.15	0.0009
5000.00	348.15	0.0010
10000.00	278.15	0.0008
10000.00	298.15	0.0008
10000.00	328.15	0.0009
10000.00	348.15	0.0010
15000.00	278.15	0.0008
15000.00	298.15	0.0008
15000.00	328.15	0.0009
15000.00	348.15	0.0009
20000.00	278.15	0.0008
20000.00	298.15	0.0008
20000.00	328.15	0.0009
20000.00	348.15	0.0009
25000.00	278.15	0.0008
25000.00	298.15	0.0008
25000.00	328.15	0.0008
25000.00	348.15	0.0009
30000.00	278.15	0.0007
30000.00	298.15	0.0008
30000.00	328.15	0.0008
30000.00	348.15	0.0009
35000.00	278.15	0.0007
35000.00	298.15	0.0007
35000.00	328.15	0.0008
35000.00	348.15	0.0008
40000.00	278.15	0.0007
40000.00	298.15	0.0007
40000.00	328.15	0.0008
40000.00	348.15	0.0008
45000.00	278.15	0.0007
45000.00	298.15	0.0007
45000.00	328.15	0.0008
45000.00	348.15	0.0008
50000.00	278.15	0.0007
50000.00	298.15	0.0007
50000.00	328.15	0.0007
50000.00	348.15	0.0008
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Isobaric coefficient of expansion, 1/K - Liquid
278.15	5000.00	0.0008
278.15	10000.00	0.0008
278.15	15000.00	0.0008
278.15	20000.00	0.0008
278.15	25000.00	0.0008
278.15	30000.00	0.0007
278.15	35000.00	0.0007
278.15	40000.00	0.0007
278.15	45000.00	0.0007
278.15	50000.00	0.0007
278.15	55000.00	0.0007
288.15	5000.00	0.0008
288.15	10000.00	0.0008
288.15	15000.00	0.0008
288.15	20000.00	0.0008
288.15	25000.00	0.0008
288.15	30000.00	0.0008
288.15	35000.00	0.0007
288.15	40000.00	0.0007
288.15	45000.00	0.0007
288.15	50000.00	0.0007
288.15	55000.00	0.0007
298.15	5000.00	0.0009
298.15	10000.00	0.0008
298.15	15000.00	0.0008
298.15	20000.00	0.0008
298.15	25000.00	0.0008
298.15	30000.00	0.0008
298.15	35000.00	0.0007
298.15	40000.00	0.0007
298.15	45000.00	0.0007
298.15	50000.00	0.0007
298.15	55000.00	0.0007
308.15	5000.00	0.0009
308.15	10000.00	0.0009
308.15	15000.00	0.0008
308.15	20000.00	0.0008
308.15	25000.00	0.0008
308.15	30000.00	0.0008
308.15	35000.00	0.0008
308.15	40000.00	0.0007
308.15	45000.00	0.0007
308.15	50000.00	0.0007
308.15	55000.00	0.0007
318.15	5000.00	0.0009
318.15	10000.00	0.0009
318.15	15000.00	0.0009
318.15	20000.00	0.0008
318.15	25000.00	0.0008
318.15	30000.00	0.0008
318.15	35000.00	0.0008
318.15	40000.00	0.0008
318.15	45000.00	0.0007
318.15	50000.00	0.0007
318.15	55000.00	0.0007
328.15	5000.00	0.0009
328.15	10000.00	0.0009
328.15	15000.00	0.0009
328.15	20000.00	0.0009
328.15	25000.00	0.0008
328.15	30000.00	0.0008
328.15	35000.00	0.0008
328.15	40000.00	0.0008
328.15	45000.00	0.0008
328.15	50000.00	0.0007
328.15	55000.00	0.0007
338.15	5000.00	0.0010
338.15	10000.00	0.0009
338.15	15000.00	0.0009
338.15	20000.00	0.0009
338.15	25000.00	0.0009
338.15	30000.00	0.0008
338.15	35000.00	0.0008
338.15	40000.00	0.0008
338.15	45000.00	0.0008
338.15	50000.00	0.0008
338.15	55000.00	0.0007
348.15	5000.00	0.0010
348.15	10000.00	0.0010
348.15	15000.00	0.0009
348.15	20000.00	0.0009
348.15	25000.00	0.0009
348.15	30000.00	0.0009
348.15	35000.00	0.0008
348.15	40000.00	0.0008
348.15	45000.00	0.0008
348.15	50000.00	0.0008
348.15	55000.00	0.0008
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	100.00	818.6
293.15	10000.00	824.8
293.15	20000.00	830.9
293.15	30000.00	836.4
293.15	40000.00	841.6
293.15	50000.00	846.5
293.15	60000.00	851.1
293.15	70000.00	855.5
293.15	80000.00	859.8
293.15	90000.00	863.7
293.15	100000.00	867.9
293.15	110000.00	871.5
293.15	120000.00	875.2
293.15	130000.00	878.7
293.15	140000.00	882.2
303.15	100.00	811.5
303.15	10000.00	818.2
303.15	20000.00	824.1
303.15	30000.00	830.0
303.15	40000.00	835.1
303.15	50000.00	840.5
303.15	60000.00	845.3
303.15	70000.00	849.8
303.15	80000.00	854.2
303.15	90000.00	858.4
303.15	100000.00	862.4
303.15	110000.00	866.3
303.15	120000.00	870.0
303.15	130000.00	873.6
303.15	140000.00	877.1
313.15	100.00	804.2
313.15	10000.00	811.1
313.15	20000.00	817.4
313.15	30000.00	823.5
313.15	40000.00	829.0
313.15	50000.00	834.4
313.15	60000.00	839.4
313.15	70000.00	844.3
313.15	80000.00	848.7
313.15	90000.00	853.1
313.15	100000.00	857.1
313.15	110000.00	861.2
313.15	120000.00	865.1
313.15	130000.00	868.7
313.15	140000.00	872.5
323.15	100.00	797.3
323.15	10000.00	804.5
323.15	20000.00	811.2
323.15	30000.00	817.4
323.15	40000.00	823.3
323.15	50000.00	828.7
323.15	60000.00	833.8
323.15	70000.00	838.5
323.15	80000.00	843.1
323.15	90000.00	847.6
323.15	100000.00	851.8
323.15	110000.00	856.0
323.15	120000.00	860.0
323.15	130000.00	863.7
323.15	140000.00	867.3
333.15	100.00	789.7
333.15	10000.00	797.2
333.15	20000.00	804.3
333.15	30000.00	810.8
333.15	40000.00	817.0
333.15	50000.00	822.7
333.15	60000.00	828.0
333.15	70000.00	832.8
333.15	80000.00	837.6
333.15	90000.00	842.5
333.15	100000.00	846.8
333.15	110000.00	850.8
333.15	120000.00	854.4
333.15	130000.00	858.5
333.15	140000.00	862.2
343.15	100.00	781.9
343.15	10000.00	790.2
343.15	20000.00	797.6
343.15	30000.00	804.4
343.15	40000.00	810.6
343.15	50000.00	816.4
343.15	60000.00	822.1
343.15	70000.00	827.3
343.15	80000.00	832.1
343.15	90000.00	836.9
343.15	100000.00	841.4
343.15	110000.00	845.7
343.15	120000.00	849.7
343.15	130000.00	853.6
343.15	140000.00	857.5
353.15	100.00	773.8
353.15	10000.00	782.3
353.15	20000.00	790.1
353.15	30000.00	797.3
353.15	40000.00	803.8
353.15	50000.00	810.0
353.15	60000.00	815.6
353.15	70000.00	821.0
353.15	80000.00	826.2
353.15	90000.00	831.1
353.15	100000.00	835.6
353.15	110000.00	840.0
353.15	120000.00	844.3
353.15	130000.00	848.4
353.15	140000.00	852.3
363.15	100.00	765.5
363.15	10000.00	774.9
363.15	20000.00	783.1
363.15	30000.00	790.6
363.15	40000.00	797.5
363.15	50000.00	803.8
363.15	60000.00	809.7
363.15	70000.00	815.4
363.15	80000.00	820.6
363.15	90000.00	825.6
363.15	100000.00	830.3
363.15	110000.00	834.8
363.15	120000.00	839.2
363.15	130000.00	843.3
363.15	140000.00	847.2
373.15	100.00	756.9
373.15	10000.00	766.6
373.15	20000.00	775.4
373.15	30000.00	783.4
373.15	40000.00	790.4
373.15	50000.00	796.9
373.15	60000.00	803.1
373.15	70000.00	808.9
373.15	80000.00	814.2
373.15	90000.00	819.5
373.15	100000.00	824.4
373.15	110000.00	829.2
373.15	120000.00	833.3
373.15	130000.00	837.7
373.15	140000.00	841.7
383.15	100.00	748.2
383.15	10000.00	759.1
383.15	20000.00	767.8
383.15	30000.00	776.5
383.15	40000.00	783.5
383.15	50000.00	790.4
383.15	60000.00	796.8
383.15	70000.00	802.6
383.15	80000.00	808.3
383.15	90000.00	813.7
383.15	100000.00	818.7
383.15	110000.00	823.4
383.15	120000.00	828.0
383.15	130000.00	832.3
383.15	140000.00	836.5
393.15	100.00	739.4
393.15	10000.00	750.8
393.15	20000.00	760.5
393.15	30000.00	768.8
393.15	40000.00	777.0
393.15	50000.00	783.7
393.15	60000.00	790.3
393.15	70000.00	796.5
393.15	80000.00	802.5
393.15	90000.00	807.8
393.15	100000.00	813.0
393.15	110000.00	818.1
393.15	120000.00	822.6
393.15	130000.00	827.2
393.15	140000.00	831.5
403.15	100.00	730.2
403.15	10000.00	741.8
403.15	20000.00	751.9
403.15	30000.00	761.1
403.15	40000.00	769.3
403.15	50000.00	776.9
403.15	60000.00	783.7
403.15	70000.00	790.1
403.15	80000.00	796.2
403.15	90000.00	801.8
403.15	100000.00	807.2
403.15	110000.00	812.3
403.15	120000.00	817.1
403.15	130000.00	821.8
403.15	140000.00	826.5
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	815.1
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
278.15	100.00	828.9
278.15	1000.00	829.5
278.15	5000.00	832.0
278.15	10000.00	835.0
278.15	15000.00	838.0
278.15	20000.00	840.8
278.15	25000.00	843.6
278.15	30000.00	846.3
278.15	35000.00	848.9
278.15	40000.00	851.4
278.15	45000.00	853.9
278.15	50000.00	856.3
278.15	55000.00	858.7
278.15	60000.00	860.9
288.15	100.00	822.1
288.15	1000.00	822.7
288.15	5000.00	825.3
288.15	10000.00	828.5
288.15	15000.00	831.6
288.15	20000.00	834.6
288.15	25000.00	837.4
288.15	30000.00	840.2
288.15	35000.00	842.9
288.15	40000.00	845.5
288.15	45000.00	848.0
288.15	50000.00	850.5
288.15	55000.00	853.0
288.15	60000.00	855.4
298.15	100.00	814.9
298.15	1000.00	815.6
298.15	5000.00	818.4
298.15	10000.00	821.7
298.15	15000.00	824.9
298.15	20000.00	828.0
298.15	25000.00	830.9
298.15	30000.00	833.8
298.15	35000.00	836.6
298.15	40000.00	839.4
298.15	45000.00	842.0
298.15	50000.00	844.6
298.15	55000.00	847.1
298.15	60000.00	849.6
308.15	100.00	807.8
308.15	1000.00	808.4
308.15	5000.00	811.4
308.15	10000.00	814.8
308.15	15000.00	818.2
308.15	20000.00	821.4
308.15	25000.00	824.5
308.15	30000.00	827.5
308.15	35000.00	830.3
308.15	40000.00	833.2
308.15	45000.00	835.9
308.15	50000.00	838.5
308.15	55000.00	841.1
308.15	60000.00	843.5
318.15	100.00	800.5
318.15	1000.00	801.2
318.15	5000.00	804.3
318.15	10000.00	807.9
318.15	15000.00	811.4
318.15	20000.00	814.7
318.15	25000.00	817.9
318.15	30000.00	821.0
318.15	35000.00	824.0
318.15	40000.00	826.9
318.15	45000.00	829.7
318.15	50000.00	832.4
318.15	55000.00	835.1
318.15	60000.00	837.7
328.15	100.00	793.0
328.15	1000.00	793.7
328.15	5000.00	797.0
328.15	10000.00	800.8
328.15	15000.00	804.4
328.15	20000.00	807.9
328.15	25000.00	811.2
328.15	30000.00	814.4
328.15	35000.00	817.6
328.15	40000.00	820.6
328.15	45000.00	823.5
328.15	50000.00	826.4
328.15	55000.00	829.1
328.15	60000.00	831.6
338.15	100.00	785.4
338.15	1000.00	786.2
338.15	5000.00	789.6
338.15	10000.00	793.6
338.15	15000.00	797.4
338.15	20000.00	801.0
338.15	25000.00	804.5
338.15	30000.00	807.9
338.15	35000.00	811.1
338.15	40000.00	814.2
338.15	45000.00	817.3
338.15	50000.00	820.2
338.15	55000.00	823.1
338.15	60000.00	825.7
348.15	100.00	777.6
348.15	1000.00	778.4
348.15	5000.00	782.0
348.15	10000.00	786.2
348.15	15000.00	790.2
348.15	20000.00	794.1
348.15	25000.00	797.6
348.15	30000.00	801.2
348.15	35000.00	804.6
348.15	40000.00	807.8
348.15	45000.00	811.0
348.15	50000.00	814.0
348.15	55000.00	817.0
348.15	60000.00	819.7
358.15	100.00	769.4
358.15	1000.00	770.0
358.15	5000.00	774.2
358.15	10000.00	778.6
358.15	15000.00	782.8
358.15	20000.00	786.9
358.15	25000.00	790.7
358.15	30000.00	794.3
358.15	35000.00	797.9
358.15	40000.00	801.3
358.15	45000.00	804.6
358.15	50000.00	807.7
358.15	55000.00	810.8
358.15	60000.00	813.5
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
278.15	100.00	828.9
278.15	1000.00	829.5
278.15	5000.00	832.0
278.15	10000.00	835.0
278.15	15000.00	838.0
278.15	20000.00	840.8
278.15	25000.00	843.6
278.15	30000.00	846.3
278.15	35000.00	848.9
278.15	40000.00	851.4
278.15	45000.00	853.9
278.15	50000.00	856.3
278.15	55000.00	858.7
278.15	60000.00	860.9
288.15	100.00	822.1
288.15	1000.00	822.7
288.15	5000.00	825.3
288.15	10000.00	828.5
288.15	15000.00	831.6
288.15	20000.00	834.6
288.15	25000.00	837.4
288.15	30000.00	840.2
288.15	35000.00	842.9
288.15	40000.00	845.5
288.15	45000.00	848.0
288.15	50000.00	850.5
288.15	55000.00	853.0
288.15	60000.00	855.4
298.15	100.00	814.9
298.15	1000.00	815.6
298.15	5000.00	818.4
298.15	10000.00	821.7
298.15	15000.00	824.9
298.15	20000.00	828.0
298.15	25000.00	830.9
298.15	30000.00	833.8
298.15	35000.00	836.6
298.15	40000.00	839.4
298.15	45000.00	842.0
298.15	50000.00	844.6
298.15	55000.00	847.1
298.15	60000.00	849.6
308.15	100.00	807.8
308.15	1000.00	808.4
308.15	5000.00	811.4
308.15	10000.00	814.8
308.15	15000.00	818.2
308.15	20000.00	821.4
308.15	25000.00	824.5
308.15	30000.00	827.5
308.15	35000.00	830.3
308.15	40000.00	833.2
308.15	45000.00	835.9
308.15	50000.00	838.5
308.15	55000.00	841.1
308.15	60000.00	843.5
318.15	100.00	800.5
318.15	1000.00	801.2
318.15	5000.00	804.3
318.15	10000.00	807.9
318.15	15000.00	811.4
318.15	20000.00	814.7
318.15	25000.00	817.9
318.15	30000.00	821.0
318.15	35000.00	824.0
318.15	40000.00	826.9
318.15	45000.00	829.7
318.15	50000.00	832.4
318.15	55000.00	835.1
318.15	60000.00	837.7
328.15	100.00	793.0
328.15	1000.00	793.7
328.15	5000.00	797.0
328.15	10000.00	800.8
328.15	15000.00	804.4
328.15	20000.00	807.9
328.15	25000.00	811.2
328.15	30000.00	814.4
328.15	35000.00	817.6
328.15	40000.00	820.6
328.15	45000.00	823.5
328.15	50000.00	826.4
328.15	55000.00	829.1
328.15	60000.00	831.6
338.15	100.00	785.4
338.15	1000.00	786.2
338.15	5000.00	789.6
338.15	10000.00	793.6
338.15	15000.00	797.4
338.15	20000.00	801.0
338.15	25000.00	804.5
338.15	30000.00	807.9
338.15	35000.00	811.1
338.15	40000.00	814.2
338.15	45000.00	817.3
338.15	50000.00	820.2
338.15	55000.00	823.1
338.15	60000.00	825.7
348.15	100.00	777.6
348.15	1000.00	778.4
348.15	5000.00	782.0
348.15	10000.00	786.2
348.15	15000.00	790.2
348.15	20000.00	794.1
348.15	25000.00	797.6
348.15	30000.00	801.2
348.15	35000.00	804.6
348.15	40000.00	807.8
348.15	45000.00	811.0
348.15	50000.00	814.0
348.15	55000.00	817.0
348.15	60000.00	819.7
358.15	100.00	769.4
358.15	1000.00	770.0
358.15	5000.00	774.2
358.15	10000.00	778.6
358.15	15000.00	782.8
358.15	20000.00	786.9
358.15	25000.00	790.7
358.15	30000.00	794.3
358.15	35000.00	797.9
358.15	40000.00	801.3
358.15	45000.00	804.6
358.15	50000.00	807.7
358.15	55000.00	810.8
358.15	60000.00	813.5
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	815.1
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
313.14	1034.00	804.9
313.14	2032.00	805.6
313.14	3046.00	806.3
313.14	4016.00	807.0
313.14	5013.00	807.7
313.14	6035.00	808.4
313.14	7010.00	809.1
313.14	8036.00	809.8
313.14	9015.00	810.5
313.14	10002.00	811.2
313.14	11020.00	811.8
313.14	12017.00	812.5
313.14	13002.00	813.2
313.14	14016.00	813.8
313.14	15016.00	814.5
313.14	16009.00	815.1
313.14	17010.00	815.8
313.14	18010.00	816.4
313.14	19012.00	817.1
313.14	20019.00	817.7
313.14	21006.00	818.3
313.14	22037.00	818.9
313.14	23037.00	819.6
313.14	24010.00	820.2
313.14	25023.00	820.8
323.12	1021.00	797.6
323.12	2009.00	798.4
323.12	3003.00	799.1
323.12	4014.00	799.8
323.12	5025.00	800.6
323.12	6021.00	801.3
323.12	7032.00	802.1
323.12	8016.00	802.8
323.12	9016.00	803.5
323.12	10019.00	804.2
323.12	11015.00	805.0
323.12	12012.00	805.7
323.12	13015.00	806.3
323.12	14006.00	807.0
323.12	15002.00	807.7
323.12	16013.00	808.4
323.12	17016.00	809.1
323.12	18018.00	809.7
323.12	19000.00	810.4
323.12	20003.00	811.0
323.12	21009.00	811.7
323.12	22000.00	812.3
323.12	23002.00	813.0
323.12	24021.00	813.6
323.12	25004.00	814.3
333.01	1023.00	790.2
333.01	2011.00	791.0
333.01	3042.00	791.8
333.01	4000.00	792.6
333.01	5014.00	793.3
333.01	6004.00	794.1
333.01	7021.00	794.9
333.01	8012.00	795.7
333.01	9002.00	796.4
333.01	10004.00	797.2
333.01	11026.00	797.9
333.01	12020.00	798.7
333.01	13018.00	799.4
333.01	14009.00	800.1
333.01	15019.00	800.8
333.01	16017.00	801.6
333.01	17006.00	802.3
333.01	18018.00	803.0
333.01	19013.00	803.7
333.01	20037.00	804.4
333.01	21029.00	805.0
333.01	22008.00	805.7
333.01	23026.00	806.4
333.01	24019.00	807.0
333.01	25025.00	807.7
342.96	1036.00	782.9
342.96	2011.00	783.7
342.96	3012.00	784.5
342.96	4015.00	785.4
342.96	5007.00	786.2
342.96	6013.00	787.0
342.96	7039.00	787.8
342.96	8023.00	788.6
342.96	9022.00	789.4
342.96	10035.00	790.2
342.96	11017.00	791.0
342.96	12016.00	791.7
342.96	13023.00	792.5
342.96	14003.00	793.2
342.96	15009.00	793.9
342.96	16014.00	794.7
342.96	17038.00	795.4
342.96	18023.00	796.1
342.96	19015.00	796.8
342.96	20015.00	797.5
342.96	21026.00	798.1
342.96	22003.00	798.8
342.96	23005.00	799.5
342.96	24003.00	800.1
342.96	25031.00	800.8
352.86	1020.00	775.0
352.86	2012.00	775.9
352.86	3028.00	776.9
352.86	4014.00	777.7
352.86	5010.00	778.6
352.86	6028.00	779.5
352.86	7039.00	780.4
352.86	8000.00	781.2
352.86	9030.00	782.1
352.86	10033.00	782.9
352.86	11014.00	783.7
352.86	12017.00	784.5
352.86	13014.00	785.3
352.86	14011.00	786.1
352.86	15010.00	786.9
352.86	16023.00	787.7
352.86	17018.00	788.5
352.86	18016.00	789.3
352.86	19014.00	790.0
352.86	20021.00	790.8
352.86	21017.00	791.5
352.86	22038.00	792.3
352.86	23016.00	793.0
352.86	24020.00	793.7
352.86	25048.00	794.5
362.80	1011.00	767.0
362.80	2009.00	768.0
362.80	3024.00	769.0
362.80	4006.00	769.9
362.80	5021.00	770.8
362.80	6035.00	771.8
362.80	7009.00	772.6
362.80	8023.00	773.6
362.80	9041.00	774.5
362.80	10000.00	775.3
362.80	11014.00	776.2
362.80	12026.00	777.1
362.80	13045.00	777.9
362.80	14030.00	778.8
362.80	15012.00	779.6
362.80	16031.00	780.4
362.80	17003.00	781.2
362.80	18020.00	782.0
362.80	19033.00	782.8
362.80	20004.00	783.6
362.80	21006.00	784.4
362.80	22032.00	785.2
362.80	22989.00	785.9
362.80	24055.00	786.7
362.80	25035.00	787.5
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
278.15	100.00	829.2
278.15	5000.00	832.2
278.15	10000.00	835.1
278.15	15000.00	837.8
278.15	20000.00	840.7
283.15	100.00	825.8
283.15	5000.00	828.7
283.15	10000.00	831.6
283.15	15000.00	834.5
283.15	20000.00	837.4
288.15	100.00	822.1
288.15	5000.00	825.2
288.15	10000.00	828.2
288.15	15000.00	831.3
288.15	20000.00	834.0
293.15	100.00	818.7
293.15	5000.00	821.9
293.15	10000.00	824.9
293.15	15000.00	827.9
293.15	20000.00	830.7
298.15	100.00	815.1
298.15	5000.00	818.3
298.15	10000.00	821.5
298.15	15000.00	824.6
298.15	20000.00	827.5
303.15	100.00	811.4
303.15	5000.00	814.8
303.15	10000.00	818.0
303.15	15000.00	821.1
303.15	20000.00	824.2
308.15	100.00	808.0
308.15	5000.00	811.3
308.15	10000.00	814.6
308.15	15000.00	817.8
308.15	20000.00	820.9
313.15	100.00	804.2
313.15	5000.00	807.6
313.15	10000.00	811.0
313.15	15000.00	814.3
313.15	20000.00	817.6
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	283.15	825.6
100.00	288.15	822.2
100.00	293.15	818.6
100.00	298.15	815.0
100.00	303.15	811.4
100.00	308.15	807.8
100.00	313.15	804.1
100.00	318.15	800.5
100.00	323.15	796.8
5000.00	283.15	828.7
5000.00	288.15	825.2
5000.00	293.15	821.7
5000.00	298.15	818.2
5000.00	303.15	814.7
5000.00	308.15	811.1
5000.00	313.15	807.6
5000.00	318.15	804.0
5000.00	323.15	800.4
10000.00	283.15	831.7
10000.00	288.15	828.2
10000.00	293.15	824.9
10000.00	298.15	821.4
10000.00	303.15	817.9
10000.00	308.15	814.5
10000.00	313.15	811.0
10000.00	318.15	807.5
10000.00	323.15	803.9
20000.00	283.15	837.3
20000.00	288.15	834.1
20000.00	293.15	830.8
20000.00	298.15	827.4
20000.00	303.15	824.1
20000.00	308.15	820.8
20000.00	313.15	817.4
20000.00	318.15	814.0
20000.00	323.15	810.7
30000.00	283.15	842.7
30000.00	288.15	839.5
30000.00	293.15	836.3
30000.00	298.15	833.1
30000.00	303.15	829.9
30000.00	308.15	826.7
30000.00	313.15	823.5
30000.00	318.15	820.1
30000.00	323.15	816.9
40000.00	283.15	847.8
40000.00	288.15	844.7
40000.00	293.15	841.6
40000.00	298.15	838.5
40000.00	303.15	835.4
40000.00	308.15	832.3
40000.00	313.15	829.1
40000.00	318.15	825.9
40000.00	323.15	822.8
50000.00	283.15	852.6
50000.00	288.15	849.6
50000.00	293.15	846.6
50000.00	298.15	843.5
50000.00	303.15	840.5
50000.00	308.15	837.5
50000.00	313.15	834.4
50000.00	318.15	831.4
50000.00	323.15	828.2
60000.00	283.15	857.2
60000.00	288.15	854.3
60000.00	293.15	851.4
60000.00	298.15	848.3
60000.00	303.15	845.4
60000.00	308.15	842.4
60000.00	313.15	839.4
60000.00	318.15	836.4
60000.00	323.15	833.4
Reference

Speed of sound, m/s

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Speed of sound, m/s - Liquid
101.00	292.91	1320.79
30390.00	292.92	1465.73
45590.00	292.92	1525.8
60790.00	292.91	1581.37
75990.00	292.92	1633.75
91180.00	292.91	1682.67
101320.00	292.91	1713.2
101.00	308.15	1269.05
15200.00	308.15	1349.81
30390.00	308.15	1419.69
45590.00	308.15	1482.88
60790.00	308.15	1540.4
75990.00	308.15	1594.13
91180.00	308.16	1643.48
101320.00	308.16	1675.87
101.00	298.18	1302.75
15200.00	298.19	1381.46
30390.00	298.19	1449.11
45590.00	298.19	1510.11
60790.00	298.19	1566.83
75990.00	298.19	1619.35
91180.00	298.19	1668.5
101320.00	298.19	1699.28
101.00	313.13	1252.38
15200.00	313.14	1334.05
30390.00	313.14	1404.76
45590.00	313.14	1469.3
60790.00	313.14	1527.64
75990.00	313.14	1581.73
91180.00	313.14	1632.08
101320.00	313.14	1664.3
101.00	318.22	1235.52
15200.00	318.22	1318.81
30390.00	318.21	1390.85
45590.00	318.21	1456.0
60790.00	318.21	1514.43
75990.00	318.21	1569.15
91180.00	318.21	1620.49
101320.00	318.21	1653.0
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[115.70; 397.23]	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			9.37330e+01
Coefficient B			-6.18920e+02
Coefficient C			6.19024e+00
Coefficient D			-2.85410e-05
Coefficient E			-8.64780e-09
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	115.70	J/mol×K	200.00	Calculated Property
Cp,gas	173.77	J/mol×K	344.44	Calculated Property
Cp,gas	229.14	J/mol×K	488.89	Calculated Property
Cp,gas	273.46	J/mol×K	633.33	Calculated Property
Cp,gas	307.97	J/mol×K	777.78	Calculated Property
Cp,gas	334.89	J/mol×K	922.22	Calculated Property
Cp,gas	356.09	J/mol×K	1066.67	Calculated Property
Cp,gas	372.94	J/mol×K	1211.11	Calculated Property
Cp,gas	386.41	J/mol×K	1355.56	Calculated Property
Cp,gas	397.23	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[197.35; 351.19]	J/mol×K	[228.55; 460.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K
Coefficient A			-1.33520e+01
Coefficient B			6.95570e+02
Coefficient C			-2.42136e+00
Coefficient D			2.65040e-02
Coefficient E			-2.54440e-05
Temperature range, min.			228.55
Temperature range, max.			460.00
Cp,liquid	197.35	J/mol×K	228.55	Calculated Property
Cp,liquid	209.91	J/mol×K	254.27	Calculated Property
Cp,liquid	228.68	J/mol×K	279.98	Calculated Property
Cp,liquid	251.31	J/mol×K	305.70	Calculated Property
Cp,liquid	275.70	J/mol×K	331.42	Calculated Property
Cp,liquid	299.75	J/mol×K	357.13	Calculated Property
Cp,liquid	321.30	J/mol×K	382.85	Calculated Property
Cp,liquid	338.24	J/mol×K	408.57	Calculated Property
Cp,liquid	348.69	J/mol×K	434.28	Calculated Property
Cp,liquid	351.19	J/mol×K	460.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0411929; 0.0000492]	Pa×s	[243.15; 611.00]	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			-7.80190e+01
Coefficient B			5.18650e+03
Coefficient C			9.83950e+00
Coefficient D			-9.40420e-06
Coefficient E			2.00000e+00
Temperature range, min.			243.15
Temperature range, max.			611.00
η	0.0411929	Pa×s	243.15	Calculated Property
η	0.0072057	Pa×s	284.02	Calculated Property
η	0.0021522	Pa×s	324.89	Calculated Property
η	0.0008897	Pa×s	365.77	Calculated Property
η	0.0004508	Pa×s	406.64	Calculated Property
η	0.0002599	Pa×s	447.51	Calculated Property
η	0.0001625	Pa×s	488.38	Calculated Property
η	0.0001067	Pa×s	529.26	Calculated Property
η	0.0000720	Pa×s	570.13	Calculated Property
η	0.0000492	Pa×s	611.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[69.18; 2.52]	kJ/mol	[228.55; 610.30]	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			9.99120e+01
Coefficient B			1.03450e+00
Coefficient C			-7.12140e-01
Coefficient D			3.88690e-02
Coefficient E			2.21030e-01
Critical temperature, Tc (K)			6.11400e+02
Temperature range, min.			228.55
Temperature range, max.			610.30
ΔvapH	69.18	kJ/mol	228.55	Calculated Property
ΔvapH	64.56	kJ/mol	270.97	Calculated Property
ΔvapH	60.01	kJ/mol	313.38	Calculated Property
ΔvapH	55.37	kJ/mol	355.80	Calculated Property
ΔvapH	50.47	kJ/mol	398.22	Calculated Property
ΔvapH	45.07	kJ/mol	440.63	Calculated Property
ΔvapH	38.85	kJ/mol	483.05	Calculated Property
ΔvapH	31.30	kJ/mol	525.47	Calculated Property
ΔvapH	21.37	kJ/mol	567.88	Calculated Property
ΔvapH	2.52	kJ/mol	610.30	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.64]	kPa	[328.27; 454.77]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.49468e+01
Coefficient B			-3.55660e+03
Coefficient C			-8.56520e+01
Temperature range, min.			328.27
Temperature range, max.			454.77
Pvap	1.33	kPa	328.27	Calculated Property
Pvap	2.98	kPa	342.33	Calculated Property
Pvap	6.11	kPa	356.38	Calculated Property
Pvap	11.68	kPa	370.44	Calculated Property
Pvap	21.02	kPa	384.49	Calculated Property
Pvap	35.88	kPa	398.55	Calculated Property
Pvap	58.48	kPa	412.60	Calculated Property
Pvap	91.57	kPa	426.66	Calculated Property
Pvap	138.38	kPa	440.71	Calculated Property
Pvap	202.64	kPa	454.77	Calculated Property
Pvap	[3.77e-05; 3294.76]	kPa	[228.55; 610.30]	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			1.33499e+02
Coefficient B			-1.19960e+04
Coefficient C			-1.68497e+01
Coefficient D			6.25688e-06
Coefficient E			2.00000e+00
Temperature range, min.			228.55
Temperature range, max.			610.30
Pvap	3.77e-05	kPa	228.55	Calculated Property
Pvap	9.05e-03	kPa	270.97	Calculated Property
Pvap	0.36	kPa	313.38	Calculated Property
Pvap	4.92	kPa	355.80	Calculated Property
Pvap	32.70	kPa	398.22	Calculated Property
Pvap	134.89	kPa	440.63	Calculated Property
Pvap	400.04	kPa	483.05	Calculated Property
Pvap	939.82	kPa	525.47	Calculated Property
Pvap	1868.72	kPa	567.88	Calculated Property
Pvap	3294.76	kPa	610.30	Calculated Property
Pvap	[5.21e-05; 3364.66]	kPa	[228.55; 611.35]	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			1.08932e+02
Coefficient B			-1.08747e+04
Coefficient C			-1.31440e+01
Coefficient D			3.48998e-06
Coefficient E			0.00000e+00
Temperature range, min.			228.55
Temperature range, max.			611.35
Pvap	5.21e-05	kPa	228.55	Calculated Property
Pvap	0.01	kPa	271.08	Calculated Property
Pvap	0.39	kPa	313.62	Calculated Property
Pvap	5.03	kPa	356.15	Calculated Property
Pvap	33.18	kPa	398.68	Calculated Property
Pvap	137.52	kPa	441.22	Calculated Property
Pvap	410.94	kPa	483.75	Calculated Property
Pvap	970.21	kPa	526.28	Calculated Property
Pvap	1926.83	kPa	568.82	Calculated Property
Pvap	3364.66	kPa	611.35	Calculated Property
Pvap	[0.76; 101.70]	kPa	[325.40; 430.50]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.47658e+01
Coefficient B			-3.27435e+03
Coefficient C			-1.07706e+02
Reference			Kemme and Kreps, 1969
Temperature range, min.			325.40
Temperature range, max.			430.50
Pvap	0.76	kPa	325.40	Calculated Property
Pvap	1.63	kPa	337.08	Calculated Property
Pvap	3.26	kPa	348.76	Calculated Property
Pvap	6.11	kPa	360.43	Calculated Property
Pvap	10.83	kPa	372.11	Calculated Property
Pvap	18.28	kPa	383.79	Calculated Property
Pvap	29.58	kPa	395.47	Calculated Property
Pvap	46.10	kPa	407.14	Calculated Property
Pvap	69.50	kPa	418.82	Calculated Property
Pvap	101.70	kPa	430.50	Calculated Property
Pvap	[1.37; 16.59]	kPa	[334.10; 381.70]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.75999e+01
Coefficient B			-4.87680e+03
Coefficient C			-5.19880e+01
Reference			Rose and Supina, 1961
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			334.10
Temperature range, max.			381.70
Pvap	1.37	kPa	334.10	Calculated Property
Pvap	1.88	kPa	339.39	Calculated Property
Pvap	2.55	kPa	344.68	Calculated Property
Pvap	3.43	kPa	349.97	Calculated Property
Pvap	4.57	kPa	355.26	Calculated Property
Pvap	6.02	kPa	360.54	Calculated Property
Pvap	7.85	kPa	365.83	Calculated Property
Pvap	10.16	kPa	371.12	Calculated Property
Pvap	13.04	kPa	376.41	Calculated Property
Pvap	16.59	kPa	381.70	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[860.20; 285.08]	kg/m3	[228.55; 610.30]	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			1.24367e+01
Coefficient B			1.12630e-01
Coefficient C			6.11400e+02
Coefficient D			1.31940e-01
Temperature range, min.			228.55
Temperature range, max.			610.30
ρl	860.20	kg/m3	228.55	Calculated Property
ρl	833.47	kg/m3	270.97	Calculated Property
ρl	804.66	kg/m3	313.38	Calculated Property
ρl	773.24	kg/m3	355.80	Calculated Property
ρl	738.45	kg/m3	398.22	Calculated Property
ρl	699.06	kg/m3	440.63	Calculated Property
ρl	652.95	kg/m3	483.05	Calculated Property
ρl	595.78	kg/m3	525.47	Calculated Property
ρl	515.50	kg/m3	567.88	Calculated Property
ρl	285.08	kg/m3	610.30	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.02]	N/m	[228.55; 430.65]	Jasper (1972), surface tension of pure liquid compounds Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K
Coefficient A			4.96893e-02
Coefficient B			-8.01000e-05
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			228.55
Temperature range, max.			430.65
γ	0.03	N/m	228.55	Calculated Property
γ	0.03	N/m	251.01	Calculated Property
γ	0.03	N/m	273.46	Calculated Property
γ	0.03	N/m	295.92	Calculated Property
γ	0.02	N/m	318.37	Calculated Property
γ	0.02	N/m	340.83	Calculated Property
γ	0.02	N/m	363.28	Calculated Property
γ	0.02	N/m	385.74	Calculated Property
γ	0.02	N/m	408.19	Calculated Property
γ	0.02	N/m	430.65	Calculated Property
γ	[0.03; 9.14e-06]	N/m	[228.55; 607.63]	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			-3.57830e-02
Coefficient B			6.68220e+01
Coefficient C			-3.06560e+00
Coefficient D			9.29640e-04
Coefficient E			-2.54400e-06
Comment			Range stopped where the equation turns negative; ChemSep gives it to 610.3 K.
Temperature range, min.			228.55
Temperature range, max.			607.63
γ	0.03	N/m	228.55	Calculated Property
γ	0.03	N/m	270.67	Calculated Property
γ	0.02	N/m	312.79	Calculated Property
γ	0.02	N/m	354.91	Calculated Property
γ	0.02	N/m	397.03	Calculated Property
γ	0.01	N/m	439.15	Calculated Property
γ	0.01	N/m	481.27	Calculated Property
γ	0.01	N/m	523.39	Calculated Property
γ	0.00	N/m	565.51	Calculated Property
γ	9.14e-06	N/m	607.63	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.11]	W/m×K	[228.55; 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			-2.14390e+06
Coefficient B			-9.29570e-02
Coefficient C			1.68200e+08
Coefficient D			-1.03390e+13
Temperature range, min.			228.55
Temperature range, max.			1000.00
λgas	0.01	W/m×K	228.55	Calculated Property
λgas	0.01	W/m×K	314.27	Calculated Property
λgas	0.02	W/m×K	399.98	Calculated Property
λgas	0.03	W/m×K	485.70	Calculated Property
λgas	0.04	W/m×K	571.42	Calculated Property
λgas	0.05	W/m×K	657.13	Calculated Property
λgas	0.06	W/m×K	742.85	Calculated Property
λgas	0.08	W/m×K	828.57	Calculated Property
λgas	0.09	W/m×K	914.28	Calculated Property
λgas	0.11	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.17; 0.09]	W/m×K	[228.55; 575.00]	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			9.20300e-02
Coefficient B			1.29760e+03
Coefficient C			-1.57120e+01
Coefficient D			4.54470e-02
Coefficient E			-5.60170e-05
Temperature range, min.			228.55
Temperature range, max.			575.00
λliquid	0.17	W/m×K	228.55	Calculated Property
λliquid	0.16	W/m×K	267.04	Calculated Property
λliquid	0.15	W/m×K	305.54	Calculated Property
λliquid	0.15	W/m×K	344.03	Calculated Property
λliquid	0.14	W/m×K	382.53	Calculated Property
λliquid	0.12	W/m×K	421.02	Calculated Property
λliquid	0.11	W/m×K	459.52	Calculated Property
λliquid	0.10	W/m×K	498.01	Calculated Property
λliquid	0.10	W/m×K	536.51	Calculated Property
λliquid	0.09	W/m×K	575.00	Calculated Property

Similar Compounds

Find more compounds similar to 1-Hexanol.

Mixtures

• Octacosanol + 1-Hexanol
• n-Hexane + 1-Hexanol
• Mercury + 1-Hexanol
• 1-Octene + 1-Hexanol
• 1-Hexanol + Furan, 2,2'-methylenebis-
• 1-Butanol + 1-Hexanol
• Acetic acid, butyl ester + 1-Hexanol
• 1-Butanol, 3-methyl- + 1-Hexanol
• Benzene, ethyl- + 1-Hexanol
• 1-Hexanol + Ethanol, 2-(2-butoxyethoxy)-
• 5-Hydroxymethylfurfural + 1-Hexanol + Water
• 1-Hexanol + Water
• Ethane, 1,1,2,2-tetrabromo- + 1-Hexanol
• 2-IMIDAZOLIDINONE, 1,3-DIMETHYL- + 1-Hexanol
• Ethanol, 2-butoxy- + 1-Hexanol
• 1-Hexanol + 1-(4-Chlorophenoxy)-1-(imidazol-1-yl)-3,3-dimethylbutanone
• Butanoic acid + 1-Hexanol + Water
• Acetonitrile + 1-Hexanol
• 2-Propenenitrile + 1-Hexanol
• Formamide, N,N-dimethyl- + 1-Hexanol

Find more mixtures with 1-Hexanol.

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).
• IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 ChEDL chemicals 1.5.2, from Gude, M.; Teja, A. S. Vapor-Liquid Critical Properties of Elements and Compounds. 4. Aliphatic Alkanols. J. Chem. Eng. Data 1995, 40, 1025-1036.
• 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).
• 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.
• Speeds of Sound and Isentropic Compressibilities in Binary Mixtures of 2-Propanol with Several 1-Alkanols at 298.15K
• Measurements of the Properties of Binary Mixtures of Dimethylsulphoxide (DMSO) with 1-Alkanols (C4, C6, C7) at 303.15K
• Densities, Excess Molar Volumes, Ultrasonic Speeds, and Isentropic Compressibilities of Hexan-1-ol with 1,2-Dichloroethane, 1,2-Dibromoethane, and 1,1,2,2-Tetrachloroethene at (293.15 and 298.15) K
• Liquid phase behavior of imidazolium-based ionic liquids with alcohols: effect of hydrogen bonding and non-polar interactions
• Phase equilibria in the ternary system isobutyl alcohol + isobutyl acetate + 1-hexanol and the binary systems isobutyl alcohol + 1-hexanol, isobutyl acetate + 1-hexanol at 101.3 kPa
• Density and surface tension variation with temperature for n-nonane + 1-hexanol
• Excess molar volumes of ternary mixtures of 1,3-dichlorobenzene and methyl ethyl ketone with 1-alkanols at 303.15K
• Phase behaviour of I-hexyloxymethyl-3-methyl-imidazolium and 1,3-dihexyloxymethyl-imidazolium based ionic liquids with alcohols, water, ketones and hydrocarbons: The effect of cation and anion on solubility
• Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
• 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
• Limiting activity coefficients in binary mixtures of 1-alkanols and ethylbenzene
• Vapour liquid equilibria, azeotropic data, excess enthalpies, activity coefficients at infinite dilution and solid liquid equilibria for binary alcohol ketone systems
• Isobaric vapour liquid equilibria of binary 1-propoxy-2-propanol mixtures with water and alcohols at reduced pressure
• Phase equilibria of (water + levunilic acid + alcohol) ternary systems
• Isobaric thermal expansivity of the binary system 1-hexanol + n-hexane as a function of temperature and pressure
• Solubility and limiting activity coefficient of simvastatin in different organic solvents
• Solubility of pyrene in simple and mixed solvent systems
• Experimental solid-liquid phase equilibria of {cholesterol + binary solvent mixture: 1-Alcohol (C4-C10) + cyclohexane}
• (Solid + liquid) and (liquid + liquid) phase equilibria study and correlation of the binary systems {N-butyl-3-methylpyridinium tosylate + water, or + an alcohol, or + a hydrocarbon}
• Temperature dependence of the excess molar volume of 1-hexanol + 1-alkene systems in terms of an association and equation of state model
• Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
• Bubble point measurements of binary mixtures formed by 1-hexanol with selected nitro-compounds and substituted benzenes at 95.6 kPa
• Liquid-liquid phase equilibrium of (piperidinium-based ionic liquid + an alcohol) binary systems and modelling with NRHB and PCP-SAFT
• Liquid density of oxygenated additives to bio-fuels: 1-Hexanol at pressures up to 140 MPa and from 293.15 K to 403.15 K
• Solubility of triclosan and iodopropynyl butylcarbamate in pure alkanols at several temperatures
• Phase behaviour of ionic liquid 1-butyl-1-methylpyrrolidinium tris(pentafluoroethyl)trifluorophosphate with alcohols, water and aromatic hydrocarbons
• Liquid-liquid equilibrium data for systems containing of formic acid, water, and primary normal alcohols at T = 298.2 K
• Liquid-liquid equilibrium data for ternary systems of water + lactic acid + C4-C7 alcohols at 298.2 K and atmospheric pressure
• (p, VE, T) Measurements of mixtures (DBE + alcohol) at temperaturesfrom (293.15 to 353.15) K and at pressures up to 140 MPa
• Unusual behavior of the isotope effect on miscibility of 1-hexyl-3-methylimidazolium bis(trifluorosulfonyl)imide with 1-alkanols
• Liquid-liquid phase equilibria of ionic liquid solutions in the critical region: 1-Methyl-3-octylimidazolium tetrafluoroborate with1-pentanol or 1-hexanol
• Measurement and correlation of the solubility of N-(phosphonomethyl)iminodiacetic acid in different organic solvents
• tert-Butyl chloride as a probe of the solvophobic effects
• Phase behaviour of tricyanomethanide-based ionic liquids with alcohols and hydrocarbons
• Atmospheric densities and interfacial tensions for 1- alkanol (1-butanol to 1-octanol) + water and ether (MTBE, ETBE, DIPE, TAME and THP) + water demixed mixtures.
• Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
• Isothermal vapor-liquid equilibria, excess molar volume and the deviation of refractive indices for binary mixtures of 1-butanol, 1- hexanol, 3-methyl-1-butanol and butyl acetate
• Solubility and dissolution characteristics of capecitabine in pure lower alcohols and water with methanol mixture solvents at atmospheric pressure and different temperatures
• Solubility determination and correlation of cyromazine in sixteen pure solvents and mixing properties of solutions
• The behavior of mercury in water, alcohols, monoethylene glycol and triethylene glycol II. Elemental mercury solubility in alcohols, ethers and acetone; gas plant mercury distribution; and speciation in monoethylene glycol solution
• Study of molecular interactions and preferential solvation in binary mixtures of cyclohexane and (C5-C10) 1-alkanol by Kirkwood-Buff integrals
• Phase equilibria for ternary liquid systems of (water + carboxylic acid or alcohol + 1-hexanol) at T = 293.15 K: modelling considerations
• Excess molar volumes and viscosities of (1,1,2,2-tetrabromoethane + 1-alkanols) at T = (293.15 and 303.15) K
• Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrachloroethane and 1-alkanols binary mixtures
• (Liquid + liquid) phase equilibria of 1-alkyl-3-methylimidazolium methylsulfate with alcohols, or ethers, or ketones
• Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrabromoethane and 1-alkanols binary mixtures
• Activity coefficients at infinite dilution and enthalpies of solution of methanol, 1-butanol, and 1-hexanol in 1-hexyl-3-methyl-imidazolium bis(trifluoromethyl-sulfonyl) imide
• Excess molar volumes of binary mixtures of 1,3-dimethylimidazolidin-2-one with an alkan-1-ol at the temperatures 283.15 K, 298.15 K, and 313.15 K
• Densities and derived thermodynamic properties of binary mixtures of diethylcarbonate, acetophenone, and 1-hexanol at T = (293.15 to 323.15) K for the liquid region and at ambient pressure
• Measurement and correlation of solubility of trans-resveratrol in 11 solvents at T = (278.2, 288.2, 298.2, 308.2, and 318.2) K
• Bubble point measurements of binary mixtures formed by ethyl benzene with selected compounds at 95.35 kPa
• 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
• Studies on thermodynamic properties of binary mixtures of hexan-1-ol with halogenated compounds at T = (308.15 and 313.15) K
• Molar excess enthalpies at T = 298.15 K for (1-alkanol + dibutylether) systems
• Isobaric thermal expansivity behaviour against temperature and pressure of associating fluids
• Volumetric, acoustic, and viscometric studies of molecular interactions in binary mixtures of diethylene glycol monomethyl ether with 1-alkanols at temperatures from (293.15 to 308.15) K
• High-pressure phase equilibria in the (carbon dioxide + 1-hexanol) system
• Ultrasonic speeds and isentropic compressibilities of {difurylmethane + (C1 C6) n-alkanol} binary mixtures at T = 298.15 K
• Cloud point measurements of 1-butyl-2,3-dimethylimidazolium tetrafluoroborate with alcohols
• Thermophysical properties and phase equilibria study of the binary systems {N-hexylquinolinium bis(trifluoromethylsulfonyl)imide + aromatic hydrocarbons, or an alcohol}
• Compressed liquid density measurements for {methylbenzoate + (cyclohexane or 1-hexanol)} binary systems
• Volumetric and viscometric properties of binary mixtures of {methyl tert-butyl ether (MTBE) + alcohol} at several temperatures and p = 0.1 MPa: Experimental results and application of the ERAS model
• Enthalpy of cooperative hydrogen bonding in complexes of tertiary amines with aliphatic alcohols: Calorimetric study
• Volumetric properties and enthalpies of solution of alcohols CkH2k+1OH (k = 1, 2, 6) in 1-methyl-3-alkylimidazolium bis(trifluoromethylsulfonyl)imide {[C1CnIm][NTf2] n = 2, 4, 6, 8, 10} ionic liquids
• Excess molar enthalpies of binary systems containing 2-octanone, hexanoic acid, or octanoic acid at T = 298.15 K
• PrhoT measurements and derived properties of liquid 1-alkanols
• Comparative study of physico-chemical properties of binary mixtures of N,N-dimethylformamide with 1-alkanols at different temperatures
• Effect of temperature and composition on the density, viscosity, surface tension, and thermodynamic properties of binary mixtures of N-octylisoquinolinium bis{(trifluoromethyl)sulfonyl}imide with alcohols
• Ternary equilibrium data of mixtures consisting of 2-butanol, water, and heavy alcohols at T = 298.2 K
• Studies of thermophysical properties of binary liquid mixtures of amine and alcohols at various temperatures
• Viscosity and surface tension of binary systems of N,N-dimethylformamide with alkan-1-ols at different temperatures
• Solubility of salicylic acid in pure alcohols at different temperatures
• Density, speed of sound, heat capacity, and related properties of 1-hexanol and 2-ethyl-1-butanol as function of temperature and pressure
• Ultrasonic study of molecular interactions in binary mixtures of methyl acrylate with 1-alkanols (C4 to C10) at temperatures from (288.15 to 318.15) K
• Volume effects for binary mixtures of propane-1,2-diol with methanol, propan-1-ol, hexan-1-ol, octan-1-ol, or nonan-1-ol at temperatures (293.15 to 318.15) K
• Ternary liquid liquid equilibrium data for the (water + butyric acid + n-hexane or n-hexanol) systems at T = (298.2, 308.2, and 318.2) K
• On the solubility of nicotinic acid and isonicotinic acid in water and organic solvents
• Study of surface tension and surface properties of binary systems of DMSO with long chain alcohols at various temperatures
• Thermodynamic, transport and excess properties of 2-butoxy ethanol +1-alkanol (C6,C8,C10) at different temperatures
• FT-IR studies on excess thermodynamic properties of binary liquid mixtures o-chlorotoluene with 1-propanol, 1-butanol, 1-pentanol, 1-hexanol and 1-heptanol at different temperatures
• Densities, speeds of sound and viscosities of binary mixtures of tetrahydrofuran with 1-hexanol, 1-octanol and 1-decanol at T = (298.15 to 313.15) K
• Application of the NRTL method to correlate solubility of diosgenin
• Solubility of climbazole in various alcohols at different temperatures
• Measurements and equation-of-state modelling of thermodynamic properties of binary mixtures of 1-butyl-1-methylpyrrolidinium tetracyanoborate ionic liquid with molecular compounds
• Volumetric and viscometric study with FT-IR analysis of binary systems with diethyl succinate and alcohols
• Solubility of commercial octacosanol in organic solvents and their correlation by thermodynamic models at different temperatures
• Physical properties of systems of interest to the edible oil industry: Viscosities and densities of model systems formed by (triacylglycerol + fatty acid + solvent)
• High pressure liquid densities and excess volumes of the (di-isopropyl ether + 1-hexanol) system
• Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
• Volumetric and transport properties of binary liquid mixtures with 1-ethyl-3-methylimidazolium ethyl sulfate as candidate solvents for regenerative flue gas desulfurization processes
• FT-IR studies and excess thermodynamic properties of binary liquid mixtures 2-(2-butoxyethoxy) ethanol with 1-hexanol, 1-octanol and 1-decanol at different temperatures
• Improving the method of solution calorimetry for evaluation of the enthalpies of phase transitions and condensed state enthalpies of formation
• Vapor-liquid equilibrium data of binary mixtures of 1-hexanol, 1-heptanol, 1-nonanol and 1,3-propanediol at P = 101.3 kPa using differential scanning calorimetry (DSC)
• The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
• Excess volumes and partial molar volumes of binary liquid mixtures of furfural or 2-methylfuran with alcohols at 298.15 K
• Liquid-liquid equilibrium for (water + 5-hydroxymethylfurfural + 1-pentanol/1-hexanol/1-heptanol) systems at 298.15 K
• Solubility and mixing thermodynamic properties of levamisole hydrochloride in twelve pure solvents at various temperatures
• Excess molar enthalpies of methyl isobutyl ketone (MIBK) with alkan-1-ols (C1-C6) and their correlations at 298.15 K
• Thermophysical properties and thermodynamic phase behavior of ionic liquids
• ERAS modeling of the excess molar enthalpies of binary liquid mixtures of 1-pentanol and 1-hexanol with acetonitrile at atmospheric pressure and 288, 298, 313 and 323K
• Excess molar enthalpies and heat capacities of dimethyl sulfoxide + seven normal alkanols at 303.15K and atmospheric pressure
• Examination of hydrogen-bonding interactions between dissolved solutes and alkylbenzene solvents based on Abraham model correlations derived from measured enthalpies of solvation
• Effect of halogen substitution on the enthalpies of solvation and hydrogen bonding of organic solutes in chlorobenzene and 1,2-dichlorobenzene derived using multi-parameter correlations
• Thermodynamic and spectral studies of molecular interactions in binary liquid mixtures of 1-butoxy-2- propanol with 1-alcohols
• Densities, Viscosities, and Refractive Indices of Dimethyl Carbonate + 1-Hexanol/1-Octanol Binary Mixtures at Different Temperatures
• Thermodynamics of 1,3-dimethylurea in eight alcohols
• Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
• Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
• Effect of Temperature on Reactive Extraction of Gallic Acid Using Tri-n-butyl Phosphate, Tri-n-octylamine and Aliquat 336
• Determination and Correlation of Solubility of Phenylbutazone in Monosolvents and Binary Solvent Mixtures
• Solubilities of 4',5,7-Triacetoxyflavanone in Fourteen Organic Solvents at Different Temperatures
• Thermodynamic Functions for Solubility of 1-Hydroxybenzotriazole in Sixteen Solvents at Temperatures from (278.15 to 313.15) K and Mixing Property of Mixtures
• Solubility and Thermodynamic Behavior of Syringic Acid in Eight Pure and Water + Methanol Mixed Solvents
• Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
• Permittivities, Refractive Indices, Densities, and Excess Properties for Binary Systems Containing 1-Alkanols and Cyclopentanone
• Solubility Modeling and Solvent Effects of Allopurinol in 15 Neat Solvents
• Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
• Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
• Comparative Dielectric Study and Molecular Interactions of Binary Mixtures of (Cyclohexanone + 1-Alkanols) and (Cyclopentanone or Cyclohexanone + Cyclohexanol or Cyclohexane) at T = 298.15 K
• Viscosities and Densities of Fatty Alcohol Mixtures from 298.15 to 338.15 K: Estimation by Kay's Rule and Prediction by the UNIFAC-VISCO and GC-UNIMOD Group Contribution Methods
• Kirkwood-Buff Integrals, Excess Volume, and Preferential Solvation in Pentanoic Acid/(C5-C10) 1-Alkanol Binary Mixtures
• Solubility Measurement and Phase Equilibrium Modeling of 2-Aminobenzamide in 15 Pure Solvents
• Solid-Liquid Equilibrium Solubility, Thermodynamic Properties, and Molecular Simulation of Phenylphosphonic Acid in 15 Pure Solvents at Different Temperatures
• Solubility Determination and Modeling of EGCG Peracetate in 12 Pure Solvents at Temperatures from 278.15 to 318.15 K
• Solubility Study and Mixing Property of 3,5-Dinitro-2-methylbenzoic Acid in 13 Pure Solvents from 288.15 to 333.15 K
• Thermodynamic Properties of 1-Hexyl-3-methylimidazolium Nitrate and 1-Alkanols Mixtures: PC-SAFT Model
• Liquid-Liquid Equilibria for Ternary Mixtures of Water + Ethanol with 1-Hexanol, Butyl Propionate, or Ethyl Caproate
• Excess Molar Enthalpies of Propyl Propanoate + 1-Hexanol + Benzene at the Temperatures of 25 :C and 35 :C
• Solubility of Benzimidazoles in Alcohols
• A Study on Properties Derived from Densities and Viscosities for the Ternary Systems (Methyl Pentanoate or Methyl Heptanoate) + n-Octane + 1-Hexanol and their Binary Subsystems at Various Temperatures.
• Density, Surface Tension, and Refractive Index of Octane + 1-Alkanol Mixtures at T ) 298.15 K.
• Heat Capacities and Derived Thermodynamic Functions of 1-Hexanol, 1-Heptanol, 1-Octanol, and 1-Decanol between 5 K and 390 K
• Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
• Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
• Liquid-Liquid Equilibria for the Ternary Systems of (Water + Tetrahydrofuran + Polar Solvent) at 298.15 K
• Liquid-Liquid Equilibrium of MTBE + Ethanol + Water and MTBE + 1-Hexanol + Water over the Temperature Range of 288.15 to 308.15 K
• Solubility and Density of 2,6-Dimethylnaphthalene in C1-C7 1-Alkanols
• Density and Relative Permittivity for 1-Alkanols + Dodecane at 298.15 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
• Phase Equlibria for Hexyl Acetate Reactive Distillation
• 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
• Densities, Viscosities, and Ultrasonic Velocity Studies of Binary Mixtures of Chloroform with Pentan-1-ol, Hexan-1-ol, and Heptan-1-ol at (303.15 and 313.15) K
• Excess Molar Enthalpies of 1,2-Propanediol + Alkan-1-ols (C1-C6) and Their Correlations at 298.15 K and Ambient Pressure (81.5 kPa)
• Henry s Constants of 1-Alkanols and 2-Ketones in Salt Solutions
• Compressed Liquid Densities and Excess Molar Volumes of CO2 + Hexan-1-ol Mixtures from (313 to 363) K and Pressures up to 25 MPa
• Density and Surface Tension Variation with Temperature for Heptane + 1-Alkanol
• Effect of Pressure on the Static Relative Permittivities of Alkan-1-ols at 298.15 K
• Experimental Study of Thermodynamic Properties of Mixtures Containing Ionic Liquid 1-Ethyl-3-methylimidazolium Ethyl Sulfate Using Gas-Liquid Chromatography and Transpiration Method
• Fluid-Phase Behavior of {1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide, [C6mim][NTf2], + C2-C8 n-Alcohol} Mixtures: Liquid-Liquid Equilibrium and Excess Volumes
• Acoustical and Excess Properties of {Chlorobenzene + 1-Hexanol, or 1-Heptanol, or 1-Octanol, or 1-Nonanol, or 1-Decanol} at (298.15, 303.15, 308.15, and 313.15) K
• Thermodynamics of Mixing Tetrahydropyran with 1-Alkanols and Excess Enthalpies of Homomorphy-Related Systems
• Viscosities and Interfacial Properties of I-Methyl-3-butylimidazolium Hexafluorophosphate and 1-Isobutenyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
• Excess Molar Enthalpies of Benzyl Alcohol + Alkanols (C1-C6) and Their Correlations at 298.15 K and Ambient Pressure
• Volumetric and Viscometric Behavior of the Binary System: (Hexan-1-ol + p-Xylene)
• Thermodynamic Parameters of Anionic Surfactant-Additive Systems at the Cloud Point
• Thermodynamics of Dissolution for Bis(triazine)-Bipyridine-Class Ligands in Different Diluents and Its Reflection on Extraction
• Density and Viscosity of the Binary Mixtures of Hexan-1-ol with Isomeric Xylenes at T = (308.15 and 318.15) K and Atmospheric Pressure
• Liquid-Liquid Phase Behavior of Solutions of 1-Hexyl-3-methylimidazolium Bis((trifluoromethyl)sulfonyl)amide (C6mimNTf2) in n-Alkyl Alcohols
• Solubilities of Phloretin in 12 Solvents at Different Temperatures
• Measurement and Study on the Liquid Liquid Equilibrium of Ionic Liquids with Aliphatic Alcohols
• Liquid Liquid Phase Equilibria of 1-Propanol + Water + n-Alcohol Ternary Systems at 298.15 K and Atmospheric Pressure
• Solubilities of Betulinic Acid in Thirteen Organic Solvents at Different Temperatures
• Liquid Liquid Phase Behavior of Solutions of 1-Butyl-3-methylimidazolium Bis((trifluoromethyl)sulfonyl)amide (C4mimNTf2) in n-Alkyl Alcohols
• Solute Partitioning Between 1-n-Butyl-3-methylimidazolium Trifluoromethanesulfonate Ionic Liquid and Supercritical CO2
• Liquid Phase Behavior of 1-Butyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide with 1-Butanol or Hexan-1-ol: Measurements of Coexistence Curves, Density, and Interfacial Tension
• Vapor Liquid Equilibrium Data for Binary Systems of 1-Methyl-4-(1-methylethenyl)-cyclohexene + {Ethanol, Propan-1-ol, Propan-2-ol, Butan-1-ol, Pentan-1-ol, or Hexan-1-ol} at 40 kPa
• Liquid Liquid Phase Behavior of Solutions of 1,3-Dimethylimidazolium- and 1-Methyl-3-propylimidazolium Bis((trifluoromethyl)sulphonyl)amide (C1,3mimNTf2) in n-Alkyl Alcohols
• Determination and Correlation of Solubilities of Lauric Acid in Eight Alcohols
• Isobaric Vapor Liquid Equilibria of Binary Systems (Propyl Acetate + 2-Methylbutan-1-ol), (Propyl Acetate + Hexan-1-ol), and (Propyl Acetate + Heptan-1-ol) at 101.3 kPa
• Comparison Study on Temperature Dependence of the Interfacial Tension of n-Alkane Water and n-Alcohol Water Two Binary Systems
• Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
• Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
• Density and Viscosity of Binary Liquid Mixtures of Ethanol + 1-Hexanol and Ethanol + 1-Heptanol from (293.15 to 328.15) K at 0.1 MPa
• Deduction of Physicochemical Properties from Solubilities: 2,4-Dihydroxybenzophenone, Biotin, and Caprolactam as Examples
• Liquid Liquid Equilibrium for Ternary Systems Containing Water, Oleic Acid, and Alcohols at 313.15 K. Effect of Alcohol Chain Length
• Densities, Viscosities, Speeds of Sound, and Refractive Indices for Binary Mixtures of Diethylcarbonate, Acetophenone, and 1-Hexanol at (293.15, 303.15, 313.15, and 323.15) K for the Liquid Region and at Ambient Pressure
• Solubilities of Betulin in Fourteen Organic Solvents at Different Temperatures
• Thermodynamics of Mixing Tetrahydrofuran with 1-Alkanols and Excess Enthalpies of Homomorphy-Related Systems
• Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
• Densities and Excess Molar Volumes of N-Methylmorpholine + 1-Alkanol Systems at 298.15 K
• Liquid Liquid Equilibria for the Quaternary Systems of Water + N-Methyl-2-pyrrolidone + 1-Hexanol + NaCl, + KCl, or + KAc
• Densities, Excess Molar Volumes, Speeds of Sound at (293.15, 298.15, and 303.15) K and Isentropic Compressibilities at 298.15 K for 1-Butanol, 1-Pentanol, or 1-Hexanol + Dibutylether Systems
• Densities, Excess Molar Volumes, and Isobaric Thermal Expansibilities for 1,2-Ethanediol + 1-Butanol, or 1-Hexanol, or 1-Octanol in the Temperature Range from (293.15 to 313.15) K
• Setup and Validation of a PGT Measuring Device. Volumetric Behavior of the Mixture 1,8-Cineole + Ethanol
• Surface Properties of Binary Mixtures of Ethylene Glycol with a Series of Aliphatic Alcohols (1-Pentanol, 1-Hexanol, and 1-Heptanol)
• Measurement and Correlation of the Solubilities of m-Phthalic Acid in Monobasic Alcohols
• Phase Equilibria Study of the Binary Systems (N-Butyl-4-methylpyridinium Tosylate Ionic Liquid + Organic Solvent, or Water)
• Thermophysical Characterization of Liquids Using Precise Density and Isobaric Heat Capacity Measurements As a Function of Pressure
• Paramagnetic Ionic Liquid 1-Butyl-3-methylimidazolium Tetrabromidocobaltate(II): Activity Coefficients at Infinite Dilution of Organic Solutes and Crystal Structure
• Thermodynamic Properties of Micellization of Sodium Dodecylbenzene Sulfonate in the Aqueous-Rich Region of 1-Pentanol and 1-Hexanol
• Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
• Vapor-Liquid Equilibria of Binary Mixtures Formed by Hexan-1-ol with Chloroethanes and Chloroethenes at 95.6 kPa
• Thermodynamic Properties of the Binary Mixture of Hexan-1-ol with m-Xylene at T = (303.15, 313.15, and 323.15) K
• Studies on Transport and Thermodynamic Properties of Binary Mixtures of Hexan-1-ol with Halogenated Compounds at 293.15 K
• Volumetric and Viscometric Properties of Binary Liquid Mixtures of Ethylene Glycol Monomethyl Ether + 1-Hexanol, 1-Octanol, and 1-Decanol at Temperatures of T = (293.15, 298.15, 303.15, and 308.15) K
• Measurement and Correlation of Solubilities of Decanedioic Acid in C4-C6 Alcohol Solvents
• Studies of Monohydric Alcohols in Aqueous Sodium Dodecyl Sulfate Solutions at T = (298.15 and 308.15) K
• Densities, Viscosities, and Volumetric Properties of Binary Mixtures of 1,2-Propanediol + 1-Heptanol or 1-Hexanol and 1,2-Ethanediol + 2-Butanol or 2-Propanol at T = (298.15, 303.15, and 308.15) K
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• NCMS SOLV-DB
• The Yaws Handbook of Vapor Pressure

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