Chemical Properties of 1-Nonanol (CAS 143-08-8)

InChI

InChI=1S/C9H20O/c1-2-3-4-5-6-7-8-9-10/h10H,2-9H2,1H3

InChI Key

ZWRUINPWMLAQRD-UHFFFAOYSA-N

Formula

C9H20O

SMILES

CCCCCCCCCO

Molecular Weight¹

144.25

CAS

143-08-8

Other Names

• 1-Hydroxynonane
• Alcohol C-9
• NSC 5521
• Nonanol-(1)
• OCTYLCARBINOL
• Octyl carbinol
• Pelargonic alcohol
• n-Nonan-1-ol
• n-Nonanol
• n-Nonyl alcohol
• nonan-1-ol
• nonanol
• nonyl alcohol

• ω : Acentric Factor.
• 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).
• 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_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_c : Critical density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I_p : Polar retention indices.
• 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.
• 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	[0.5841; 0.6177]
ω	0.6177		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.5841		ChemSep v8.3 pure component data Compiled value
ΔcH°liquid	[-5947.00; -5939.48]	kJ/mol
ΔcH°liquid	-5946.30 ± 0.60	kJ/mol	NIST
ΔcH°liquid	-5947.00 ± 1.00	kJ/mol	NIST
ΔcH°liquid	-5940.80 ± 1.00	kJ/mol	NIST
ΔcH°liquid	-5939.50 ± 3.00	kJ/mol	NIST
ΔcH°liquid	-5939.48	kJ/mol	NIST
μ	[1.61; 1.70]	debye
μ	1.61	debye	ChemSep v8.3 pure component data Compiled value
μ	1.70	debye	KDB
LFL	0.80	% in Air	KDB
UFL	6.10	% in Air	KDB
Tflash,cc	372.04	K	KDB
Tflash,oc	347.04	K	KDB
ΔfG°	-108.60	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	[-387.20; -368.70]	kJ/mol
ΔfH°gas	-377.90	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-387.20	kJ/mol	KDB
ΔfH°gas	-368.70	kJ/mol	NIST
ΔfH°gas	-376.70 ± 1.00	kJ/mol	NIST
ΔfH°gas	-376.00 ± 1.30	kJ/mol	NIST
ΔfH°gas	-374.30	kJ/mol	NIST
ΔfH°gas	-382.30 ± 1.40	kJ/mol	NIST
ΔfH°gas	-375.60 ± 2.10	kJ/mol	NIST
ΔfH°gas	-383.50 ± 3.10	kJ/mol	NIST
ΔfH°liquid	[-460.50; -453.60]	kJ/mol
ΔfH°liquid	-453.60 ± 0.60	kJ/mol	NIST
ΔfH°liquid	-459.20 ± 1.20	kJ/mol	NIST
ΔfH°liquid	-460.50 ± 3.00	kJ/mol	NIST
ΔfH°liquid	-460.40 ± 3.00	kJ/mol	NIST
ΔfusH°	23.15	kJ/mol	Joback Calculated Property
ΔvapH°	[72.20; 84.90]	kJ/mol
ΔvapH°	76.86	kJ/mol	NIST
ΔvapH°	74.70 ± 0.30	kJ/mol	NIST
ΔvapH°	72.20	kJ/mol	NIST
ΔvapH°	76.70	kJ/mol	NIST
ΔvapH°	77.40	kJ/mol	NIST
ΔvapH°	76.86 ± 0.75	kJ/mol	NIST
ΔvapH°	76.90 ± 0.80	kJ/mol	NIST
ΔvapH°	77.80 ± 1.90	kJ/mol	NIST
ΔvapH°	Outlier 84.90	kJ/mol	NIST
IE	9.92	eV	Relay (1.0) Calculated Property
log10WS	[-3.01; -3.01]
log10WS	-3.01		Aq. Solubility Prediction
log10WS	-3.01		Estimated Solubility
logPoct/wat	2.729		Crippen Calculated Property
McVol	143.540	ml/mol	McGowan Calculated Property
NFPA Fire	2		KDB
NFPA Health	1		KDB
Pc	[2510.00; 2546.00]	kPa
Pc	2528.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Pc	2546.00	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	2527.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	2528.00	kPa	KDB
Pc	2530.00 ± 50.00	kPa	NIST
Pc	2510.00 ± 60.00	kPa	NIST
Pc	2546.00 ± 20.00	kPa	NIST
Pc	2546.00 ± 20.00	kPa	NIST
Ptriple	8.55e-05	kPa	ChemSep v8.3 pure component data Compiled value
ρc	[252.45; 265.43]	kg/m3
ρc	252.45 ± 7.21	kg/m3	NIST
ρc	263.99	kg/m3	NIST
ρc	252.45 ± 5.77	kg/m3	NIST
ρc	265.43 ± 2.89	kg/m3	NIST
Inp	[195.98; 1186.00]
Inp	1157.20		NIST
Inp	1156.90		NIST
Inp	1173.00		NIST
Inp	1172.00		NIST
Inp	1161.90		NIST
Inp	1161.30		NIST
Inp	1153.60		NIST
Inp	1149.00		NIST
Inp	1147.00		NIST
Inp	1143.00		NIST
Inp	1140.00		NIST
Inp	1140.00		NIST
Inp	1167.00		NIST
Inp	1154.00		NIST
Inp	1160.00		NIST
Inp	1162.00		NIST
Inp	1143.00		NIST
Inp	1166.00		NIST
Inp	1160.00		NIST
Inp	1162.00		NIST
Inp	1160.00		NIST
Inp	1160.00		NIST
Inp	1151.00		NIST
Inp	1152.00		NIST
Inp	1163.00		NIST
Inp	1161.00		NIST
Inp	1186.00		NIST
Inp	1172.00		NIST
Inp	1172.00		NIST
Inp	1169.20		NIST
Inp	1149.00		NIST
Inp	1149.00		NIST
Inp	1181.00		NIST
Inp	1175.00		NIST
Inp	1171.00		NIST
Inp	1168.00		NIST
Inp	1180.00		NIST
Inp	1151.00		NIST
Inp	1173.00		NIST
Inp	1154.50		NIST
Inp	1171.40		NIST
Inp	1171.00		NIST
Inp	1137.00		NIST
Inp	1163.00		NIST
Inp	1166.00		NIST
Inp	1169.00		NIST
Inp	1171.00		NIST
Inp	1175.00		NIST
Inp	1155.00		NIST
Inp	1163.30		NIST
Inp	1171.00		NIST
Inp	1156.70		NIST
Inp	1156.80		NIST
Inp	1156.80		NIST
Inp	1156.90		NIST
Inp	1169.00		NIST
Inp	1160.00		NIST
Inp	1171.60		NIST
Inp	1179.00		NIST
Inp	1173.90		NIST
Inp	1172.00		NIST
Inp	1174.00		NIST
Inp	1153.00		NIST
Inp	1169.00		NIST
Inp	1170.00		NIST
Inp	1154.00		NIST
Inp	1154.00		NIST
Inp	1171.00		NIST
Inp	1173.00		NIST
Inp	1175.00		NIST
Inp	1150.00		NIST
Inp	1173.00		NIST
Inp	1156.00		NIST
Inp	1170.00		NIST
Inp	1158.00		NIST
Inp	1173.00		NIST
Inp	1174.00		NIST
Inp	1176.00		NIST
Inp	1171.00		NIST
Inp	1174.00		NIST
Inp	1172.00		NIST
Inp	1156.00		NIST
Inp	1163.00		NIST
Inp	1171.00		NIST
Inp	1154.00		NIST
Inp	1173.00		NIST
Inp	1155.00		NIST
Inp	1159.00		NIST
Inp	1178.00		NIST
Inp	1161.00		NIST
Inp	1155.00		NIST
Inp	1155.00		NIST
Inp	1153.00		NIST
Inp	1160.00		NIST
Inp	1155.00		NIST
Inp	1174.00		NIST
Inp	1173.00		NIST
Inp	1180.00		NIST
Inp	1181.00		NIST
Inp	1181.00		NIST
Inp	1176.00		NIST
Inp	1174.00		NIST
Inp	1173.00		NIST
Inp	1171.00		NIST
Inp	1171.00		NIST
Inp	1172.00		NIST
Inp	1186.00		NIST
Inp	1183.00		NIST
Inp	1169.00		NIST
Inp	1176.00		NIST
Inp	1182.00		NIST
Inp	1182.00		NIST
Inp	1156.00		NIST
Inp	1166.00		NIST
Inp	1157.00		NIST
Inp	1161.00		NIST
Inp	1159.00		NIST
Inp	1160.00		NIST
Inp	1180.00		NIST
Inp	1152.00		NIST
Inp	1155.00		NIST
Inp	1157.00		NIST
Inp	1157.00		NIST
Inp	1161.00		NIST
Inp	1161.00		NIST
Inp	1164.00		NIST
Inp	Outlier 195.98		NIST
Inp	Outlier 197.48		NIST
Inp	Outlier 196.63		NIST
Inp	1186.00		NIST
Inp	1171.00		NIST
Inp	1156.00		NIST
Inp	1176.00		NIST
Inp	1163.00		NIST
Inp	1159.00		NIST
Inp	1153.00		NIST
Inp	1155.00		NIST
Inp	1181.00		NIST
Inp	1157.00		NIST
Inp	1152.00		NIST
Inp	1161.00		NIST
Inp	Outlier 195.98		NIST
Ip	[1619.00; 1695.00]
Ip	1662.00		NIST
Ip	1649.00		NIST
Ip	Outlier 1627.00		NIST
Ip	1658.00		NIST
Ip	1659.00		NIST
Ip	1652.00		NIST
Ip	1664.00		NIST
Ip	1680.00		NIST
Ip	1663.00		NIST
Ip	Outlier 1624.00		NIST
Ip	1635.00		NIST
Ip	1630.00		NIST
Ip	1665.00		NIST
Ip	1647.00		NIST
Ip	Outlier 1624.00		NIST
Ip	1640.00		NIST
Ip	Outlier 1624.00		NIST
Ip	1629.00		NIST
Ip	1655.00		NIST
Ip	1655.00		NIST
Ip	1663.00		NIST
Ip	1666.00		NIST
Ip	1666.00		NIST
Ip	1662.00		NIST
Ip	1666.00		NIST
Ip	1673.00		NIST
Ip	1658.00		NIST
Ip	1656.00		NIST
Ip	1654.00		NIST
Ip	1643.00		NIST
Ip	1640.00		NIST
Ip	1668.00		NIST
Ip	1649.00		NIST
Ip	1682.00		NIST
Ip	1661.00		NIST
Ip	1663.00		NIST
Ip	1644.00		NIST
Ip	1653.00		NIST
Ip	1671.00		NIST
Ip	1668.00		NIST
Ip	1663.30		NIST
Ip	1663.90		NIST
Ip	1663.90		NIST
Ip	1664.80		NIST
Ip	1665.00		NIST
Ip	1665.00		NIST
Ip	1666.00		NIST
Ip	1645.00		NIST
Ip	1668.00		NIST
Ip	1663.00		NIST
Ip	1639.00		NIST
Ip	1653.00		NIST
Ip	1665.00		NIST
Ip	1649.00		NIST
Ip	1681.20		NIST
Ip	1681.20		NIST
Ip	1645.00		NIST
Ip	1661.00		NIST
Ip	1661.00		NIST
Ip	1669.00		NIST
Ip	1660.00		NIST
Ip	Outlier 1625.00		NIST
Ip	1647.00		NIST
Ip	1658.00		NIST
Ip	1662.00		NIST
Ip	1665.00		NIST
Ip	1658.00		NIST
Ip	Outlier 1619.00		NIST
Ip	1657.00		NIST
Ip	1636.00		NIST
Ip	1665.00		NIST
Ip	1658.00		NIST
Ip	1674.00		NIST
Ip	Outlier 1624.00		NIST
Ip	1664.00		NIST
Ip	1664.00		NIST
Ip	1664.00		NIST
Ip	1661.00		NIST
Ip	1676.00		NIST
Ip	1685.00		NIST
Ip	1653.00		NIST
Ip	1653.00		NIST
Ip	1649.00		NIST
Ip	Outlier 1695.00		NIST
Ip	1652.00		NIST
Ip	1660.00		NIST
Ip	1654.00		NIST
Ip	1660.00		NIST
Ip	1665.00		NIST
Ip	Outlier 1695.00		NIST
Ip	1647.00		NIST
Ip	1650.00		NIST
Ip	1661.00		NIST
Ip	1664.00		NIST
Ip	1661.00		NIST
Ip	1649.00		NIST
Ip	1660.00		NIST
Ip	1673.00		NIST
Ip	1640.00		NIST
Ip	1663.00		NIST
Ip	1663.30		NIST
Ip	1665.00		NIST
Ip	1662.00		NIST
Ip	1652.00		NIST
Ip	1635.00		NIST
Tboil	[471.55; 488.40]	K
Tboil	488.40	K	(Liquid + liquid) equilibria of (water + propionic acid + alcohol) ternary systems
Tboil	488.40	K	(Liquid + liquid) equilibria of (water + lactic acid + alcohol) ternary systems
Tboil	486.55	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	485.20	K	ChemSep v8.3 pure component data Compiled value
Tboil	486.52	K	KDB
Tboil	488.20	K	NIST
Tboil	486.70	K	NIST
Tboil	486.25 ± 1.00	K	NIST
Tboil	486.45 ± 0.50	K	NIST
Tboil	Outlier 471.55 ± 2.00	K	NIST
Tboil	486.40 ± 3.00	K	NIST
Tboil	486.65 ± 0.50	K	NIST
Tboil	486.15 ± 4.00	K	NIST
Tboil	486.15 ± 3.00	K	NIST
Tboil	486.65 ± 2.00	K	NIST
Tc	[670.40; 683.00]	K
Tc	670.70	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Tc	671.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	670.90	K	ChemSep v8.3 pure component data Compiled value
Tc	670.70	K	KDB
Tc	671.00 ± 1.00	K	NIST
Tc	671.30 ± 1.00	K	NIST
Tc	670.40 ± 0.60	K	NIST
Tc	670.40 ± 0.60	K	NIST
Tc	670.50	K	NIST
Tc	670.52 ± 0.70	K	NIST
Tc	Outlier 683.00 ± 2.00	K	NIST
Tfus	[267.55; 268.15]	K
Tfus	268.10	K	Experimental (Solid + Liquid) and (Liquid + Liquid) Equilibria and Excess Molar Volume of Alkanol + Acetonitrile, Propanenitrile, and Butanenitrile Mixtures
Tfus	268.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	268.15	K	ChemSep v8.3 pure component data Compiled value
Tfus	268.00	K	KDB
Tfus	267.55	K	Aq. Solubility Prediction
Ttriple	268.15	K	ChemSep v8.3 pure component data Compiled value
UQi	6.37		ChemSep v8.3 pure component data Compiled value
URi	7.30		ChemSep v8.3 pure component data Compiled value
Vc	[0.544; 0.576]	m3/kmol
Vc	0.572	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Vc	0.544	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.576	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.572	m3/kmol	KDB
Vc	0.572	m3/kmol	NIST
Zc	[0.2593030; 0.2610000]
Zc	0.2600000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Zc	0.2610000		ChemSep v8.3 pure component data Compiled value
Zc	0.2593030		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[342.90; 356.30]	J/mol×K	[303.10; 304.17]
Cp,liquid	356.30	J/mol×K	303.10	NIST
Cp,liquid	342.90	J/mol×K	304.17	NIST
η	[0.0022560; 0.0174390]	Pa×s	[283.15; 348.15]
η	0.0174390	Pa×s	283.15	Density and Viscosity of the Binary Systems Ethanol + Butan-1-ol, + Pentan-1-ol, + Heptan-1-ol, + Octan-1-ol, Nonan-1-ol, + Decan-1-ol at 0.1 MPa and Temperatures from 283.15 K to 313.15 K
η	0.0174390	Pa×s	283.15	Measurement of Density and Viscosity of Binary 1-Alkanol Systems (C8-C11) at 101 kPa and Temperatures from (283.15 to 313.15) K
η	0.0142720	Pa×s	288.15	Measurement of Density and Viscosity of Binary 1-Alkanol Systems (C8-C11) at 101 kPa and Temperatures from (283.15 to 313.15) K
η	0.0116350	Pa×s	293.15	Measurement of Density and Viscosity of Binary 1-Alkanol Systems (C8-C11) at 101 kPa and Temperatures from (283.15 to 313.15) K
η	0.0116830	Pa×s	293.15	Densities and Kinematic Viscosities of Ten Binary 1-Alkanol Liquid Systems at Temperatures of (293.15 and 298.15) K
η	0.0116350	Pa×s	293.15	Density and Viscosity of the Binary Systems Ethanol + Butan-1-ol, + Pentan-1-ol, + Heptan-1-ol, + Octan-1-ol, Nonan-1-ol, + Decan-1-ol at 0.1 MPa and Temperatures from 283.15 K to 313.15 K
η	0.0093430	Pa×s	298.15	Density and Viscosity of Binary Mixtures of {1-Butyl-3-methylimidazolium Thiocyanate + 1-Heptanol, 1-Octanol, 1-Nonanol, or 1-Decanol}
η	0.0096710	Pa×s	298.15	Densities and Kinematic Viscosities of Ten Binary 1-Alkanol Liquid Systems at Temperatures of (293.15 and 298.15) K
η	0.0097150	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	0.0095190	Pa×s	298.15	Density and Viscosity of the Binary Systems Ethanol + Butan-1-ol, + Pentan-1-ol, + Heptan-1-ol, + Octan-1-ol, Nonan-1-ol, + Decan-1-ol at 0.1 MPa and Temperatures from 283.15 K to 313.15 K
η	0.0095190	Pa×s	298.15	Measurement of Density and Viscosity of Binary 1-Alkanol Systems (C8-C11) at 101 kPa and Temperatures from (283.15 to 313.15) K
η	0.0079270	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	0.0078060	Pa×s	303.15	Density and Viscosity of the Binary Systems Ethanol + Butan-1-ol, + Pentan-1-ol, + Heptan-1-ol, + Octan-1-ol, Nonan-1-ol, + Decan-1-ol at 0.1 MPa and Temperatures from 283.15 K to 313.15 K
η	0.0078060	Pa×s	303.15	Measurement of Density and Viscosity of Binary 1-Alkanol Systems (C8-C11) at 101 kPa and Temperatures from (283.15 to 313.15) K
η	0.0066640	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	0.0064970	Pa×s	308.15	Density and Viscosity of Binary Mixtures of {1-Butyl-3-methylimidazolium Thiocyanate + 1-Heptanol, 1-Octanol, 1-Nonanol, or 1-Decanol}
η	0.0066040	Pa×s	308.15	Measurement of Density and Viscosity of Binary 1-Alkanol Systems (C8-C11) at 101 kPa and Temperatures from (283.15 to 313.15) K
η	0.0056680	Pa×s	313.15	Measurement of Density and Viscosity of Binary 1-Alkanol Systems (C8-C11) at 101 kPa and Temperatures from (283.15 to 313.15) K
η	0.0056680	Pa×s	313.15	Density and Viscosity of the Binary Systems Ethanol + Butan-1-ol, + Pentan-1-ol, + Heptan-1-ol, + Octan-1-ol, Nonan-1-ol, + Decan-1-ol at 0.1 MPa and Temperatures from 283.15 K to 313.15 K
η	0.0056450	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	0.0046740	Pa×s	318.15	Density and Viscosity of Binary Mixtures of {1-Butyl-3-methylimidazolium Thiocyanate + 1-Heptanol, 1-Octanol, 1-Nonanol, or 1-Decanol}
η	0.0034520	Pa×s	328.15	Density and Viscosity of Binary Mixtures of {1-Butyl-3-methylimidazolium Thiocyanate + 1-Heptanol, 1-Octanol, 1-Nonanol, or 1-Decanol}
η	0.0026640	Pa×s	338.15	Density and Viscosity of Binary Mixtures of {1-Butyl-3-methylimidazolium Thiocyanate + 1-Heptanol, 1-Octanol, 1-Nonanol, or 1-Decanol}
η	0.0022560	Pa×s	348.15	Density and Viscosity of Binary Mixtures of {1-Butyl-3-methylimidazolium Thiocyanate + 1-Heptanol, 1-Octanol, 1-Nonanol, or 1-Decanol}
ΔvapH	[54.39; 65.50]	kJ/mol	[426.00; 486.60]
ΔvapH	65.50	kJ/mol	426.00	NIST
ΔvapH	64.50	kJ/mol	427.50	NIST
ΔvapH	65.00	kJ/mol	434.00	NIST
ΔvapH	62.90	kJ/mol	438.00	NIST
ΔvapH	59.70	kJ/mol	459.50	NIST
ΔvapH	54.39	kJ/mol	486.60	KDB
Pvap	[8.60e-04; 101.30]	kPa	[284.30; 486.55]
Pvap	8.60e-04	kPa	284.30	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	1.36e-03	kPa	288.20	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	2.20e-03	kPa	292.20	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	3.38e-03	kPa	296.20	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	5.09e-03	kPa	300.20	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	7.05e-03	kPa	304.20	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	0.01	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	0.01	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	0.01	kPa	311.30	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	0.02	kPa	313.30	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	0.02	kPa	314.30	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	0.02	kPa	317.20	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	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	0.03	kPa	320.30	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	0.04	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	0.04	kPa	323.30	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	0.05	kPa	326.20	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	326.30	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	0.06	kPa	329.20	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	0.06	kPa	329.30	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	0.08	kPa	332.20	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	0.08	kPa	332.30	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	335.40	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	0.12	kPa	338.30	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	0.16	kPa	341.20	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	0.20	kPa	344.30	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	0.24	kPa	347.30	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	0.31	kPa	350.30	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	0.38	kPa	353.40	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	101.30	kPa	486.55	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)
n0	[1.43084; 1.43340]		[293.15; 298.15]
n0	1.43300		293.15	Effect of temperature and chain length on the viscosity and surface tension of binary systems of N,N-dimethylformamide with 1-octanol, 1-nonanol and 1-decanol
n0	1.43340		293.15	Experimental solubility for betulin and estrone in various solvents within the temperature range T = (293.2 to 328.2) K
n0	1.43270		293.15	Distribution of Butyric Acid between Water and Several Solvents
n0	1.43220		295.10	Ternary Liquid-Liquid Equilibria of Acetonitrile and Water with Heptanoic Acid and Nonanol at 323.15 K and 1 atm
n0	1.43230		298.15	Thermodynamic and transport properties of (1,2-ethanediol + 1-nonanol) at temperatures from (298.15 to 313.15) K
n0	1.43084		298.15	Liquid Liquid Phase Equilibria of 1-Propanol + Water + n-Alcohol Ternary Systems at 298.15 K and Atmospheric Pressure
ρl	[777.76; 834.71]	kg/m3	[283.15; 363.15]
ρl	834.71	kg/m3	283.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl	831.33	kg/m3	288.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl	828.00	kg/m3	293.00	KDB
ρl	828.00	kg/m3	293.15	Influence of chlorine atom on interactions between halo-hydrocarbons and 1-nonanol: Density and speed of sound measurements
ρl	827.50	kg/m3	293.15	Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl	827.50	kg/m3	293.15	Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl	827.67	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	827.65	kg/m3	293.15	Densities, Speeds of Sound, and Isentropic Compressibilities for Binary Mixtures of 1,2-Ethanediol with 2-Ethyl-1-hexanol, 1-Heptanol, or Ethanol at the Temperature 298.15 K and Densities for Mixtures of 1,2-Ethanediol with 1-Nonanol at the Temperatures (293.15 and 298.15) K
ρl	827.93	kg/m3	293.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl	827.66	kg/m3	293.15	Speeds of Sound, Densities, Isobaric Thermal Expansion, Compressibilities, and Internal Pressures of Heptan-1-ol, Octan-1-ol, Nonan-1-ol, and Decan-1-ol at Temperatures from (293 to 318) K and Pressures up to 100 MPa
ρl	824.52	kg/m3	298.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl	824.27	kg/m3	298.15	Acoustic and thermodynamic properties of binary mixtures of 1-nonanol with o-xylene, m-xylene, p-xylene, ethylbenzene and mesitylene at T = (298.15 and 308.15) K
ρl	824.24	kg/m3	298.15	Densities, Speeds of Sound, and Isentropic Compressibilities for Binary Mixtures of 1,2-Ethanediol with 2-Ethyl-1-hexanol, 1-Heptanol, or Ethanol at the Temperature 298.15 K and Densities for Mixtures of 1,2-Ethanediol with 1-Nonanol at the Temperatures (293.15 and 298.15) K
ρl	824.00	kg/m3	298.15	Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl	824.00	kg/m3	298.15	Influence of chlorine atom on interactions between halo-hydrocarbons and 1-nonanol: Density and speed of sound measurements
ρl	824.48	kg/m3	298.15	Physico-chemical properties of binary mixtures of N,N-dimethylformamide with 1-octanol, 1-nonanol and 1-decanol at different temperatures
ρl	823.90	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	824.51	kg/m3	298.15	Effect of chain length of alcohol on thermodynamic properties of their binary mixtures with benzylalcohol
ρl	824.60	kg/m3	298.15	Experimental Solid + Liquid Equilibria and Excess Molar Volume of Alkanol + Octylamine Mixtures. Analysis in Terms of ERAS, DISQUAC, and Modified UNIFAC
ρl	824.26	kg/m3	298.15	Density and Relative Permittivity for 1-Alkanols + Dodecane at 298.15 K
ρl	824.25	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	824.00	kg/m3	298.15	Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl	824.24	kg/m3	298.15	Speeds of Sound, Densities, Isobaric Thermal Expansion, Compressibilities, and Internal Pressures of Heptan-1-ol, Octan-1-ol, Nonan-1-ol, and Decan-1-ol at Temperatures from (293 to 318) K and Pressures up to 100 MPa
ρl	821.07	kg/m3	303.15	Effect of chain length of alcohol on thermodynamic properties of their binary mixtures with benzylalcohol
ρl	821.36	kg/m3	303.15	Studies on the importance of chain length of alkanols on the thermodynamic and transport properties of liquid mixtures at various temperatures
ρl	821.09	kg/m3	303.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl	820.50	kg/m3	303.15	Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl	821.00	kg/m3	303.15	Influence of chlorine atom on interactions between halo-hydrocarbons and 1-nonanol: Density and speed of sound measurements
ρl	820.82	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	820.50	kg/m3	303.15	Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl	820.80	kg/m3	303.16	Speeds of Sound, Densities, Isobaric Thermal Expansion, Compressibilities, and Internal Pressures of Heptan-1-ol, Octan-1-ol, Nonan-1-ol, and Decan-1-ol at Temperatures from (293 to 318) K and Pressures up to 100 MPa
ρl	817.10	kg/m3	308.15	Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl	817.36	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	817.51	kg/m3	308.15	Effect of chain length of alcohol on thermodynamic properties of their binary mixtures with benzylalcohol
ρl	817.10	kg/m3	308.15	Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl	817.00	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	818.00	kg/m3	308.15	Influence of chlorine atom on interactions between halo-hydrocarbons and 1-nonanol: Density and speed of sound measurements
ρl	817.36	kg/m3	308.15	Acoustic and thermodynamic properties of binary mixtures of 1-nonanol with o-xylene, m-xylene, p-xylene, ethylbenzene and mesitylene at T = (298.15 and 308.15) K
ρl	817.54	kg/m3	308.15	Studies on the importance of chain length of alkanols on the thermodynamic and transport properties of liquid mixtures at various temperatures
ρl	817.65	kg/m3	308.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl	817.35	kg/m3	308.15	Speeds of Sound, Densities, Isobaric Thermal Expansion, Compressibilities, and Internal Pressures of Heptan-1-ol, Octan-1-ol, Nonan-1-ol, and Decan-1-ol at Temperatures from (293 to 318) K and Pressures up to 100 MPa
ρl	814.04	kg/m3	313.15	Effect of chain length of alcohol on thermodynamic properties of their binary mixtures with benzylalcohol
ρl	813.60	kg/m3	313.15	Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl	813.60	kg/m3	313.15	Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl	814.18	kg/m3	313.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl	813.88	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	814.05	kg/m3	313.15	Studies on the importance of chain length of alkanols on the thermodynamic and transport properties of liquid mixtures at various temperatures
ρl	813.87	kg/m3	313.15	Speeds of Sound, Densities, Isobaric Thermal Expansion, Compressibilities, and Internal Pressures of Heptan-1-ol, Octan-1-ol, Nonan-1-ol, and Decan-1-ol at Temperatures from (293 to 318) K and Pressures up to 100 MPa
ρl	810.10	kg/m3	318.15	Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl	810.69	kg/m3	318.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl	810.10	kg/m3	318.15	Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl	810.38	kg/m3	318.15	Speeds of Sound, Densities, Isobaric Thermal Expansion, Compressibilities, and Internal Pressures of Heptan-1-ol, Octan-1-ol, Nonan-1-ol, and Decan-1-ol at Temperatures from (293 to 318) K and Pressures up to 100 MPa
ρl	810.38	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	808.97	kg/m3	318.15	Studies on the importance of chain length of alkanols on the thermodynamic and transport properties of liquid mixtures at various temperatures
ρl	810.00	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	806.50	kg/m3	323.15	Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl	807.17	kg/m3	323.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl	806.50	kg/m3	323.15	Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl	802.90	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	803.62	kg/m3	328.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl	800.04	kg/m3	333.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl	795.70	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	796.42	kg/m3	338.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl	792.77	kg/m3	343.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl	789.07	kg/m3	348.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl	785.35	kg/m3	353.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl	781.57	kg/m3	358.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl	777.76	kg/m3	363.15	Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
csound,fluid	[1314.00; 1381.00]	m/s	[293.15; 313.15]
csound,fluid	1381.00	m/s	293.15	Densities, Speeds of Sound, and Isentropic Compressibilities of Binary Mixtures of {Alkan-1-ols + 1,2-Dimethylbenzene, or 1,3-Dimethylbenzene, or 1,4-Dimethylbenzene, or Ethylbenzene} at (293.15, 303.15, and 313.15) K
csound,fluid	1364.53	m/s	298.15	Micellar Properties and Related Thermodynamic Parameters of Aqueous Anionic Surfactants in the Presence of Monohydric Alcohols
csound,fluid	1364.47	m/s	298.15	Densities, Speeds of Sound, and Isentropic Compressibilities for Binary Mixtures of 2-Ethyl-1-hexanol with 1-Pentanol, 1-Heptanol, or 1-Nonanol at the Temperature 298.15 K
csound,fluid	1347.00	m/s	303.15	Densities, Speeds of Sound, and Isentropic Compressibilities of Binary Mixtures of {Alkan-1-ols + 1,2-Dimethylbenzene, or 1,3-Dimethylbenzene, or 1,4-Dimethylbenzene, or Ethylbenzene} at (293.15, 303.15, and 313.15) K
csound,fluid	1347.59	m/s	303.15	Micellar Properties and Related Thermodynamic Parameters of Aqueous Anionic Surfactants in the Presence of Monohydric Alcohols
csound,fluid	1331.00	m/s	308.15	Micellar Properties and Related Thermodynamic Parameters of Aqueous Anionic Surfactants in the Presence of Monohydric Alcohols
csound,fluid	1314.00	m/s	313.15	Densities, Speeds of Sound, and Isentropic Compressibilities of Binary Mixtures of {Alkan-1-ols + 1,2-Dimethylbenzene, or 1,3-Dimethylbenzene, or 1,4-Dimethylbenzene, or Ethylbenzene} at (293.15, 303.15, and 313.15) K
γ	0.03	N/m	293.20	KDB

Datasets

1. Isobaric coefficient of expansion, 1/K (1)
2. Mass density, kg/m3 (4)

Isobaric coefficient of expansion, 1/K

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	0.0007
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	0.0007
288.15	30000.00	0.0007
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	0.0008
298.15	10000.00	0.0008
298.15	15000.00	0.0008
298.15	20000.00	0.0008
298.15	25000.00	0.0007
298.15	30000.00	0.0007
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	0.0008
308.15	10000.00	0.0008
308.15	15000.00	0.0008
308.15	20000.00	0.0008
308.15	25000.00	0.0008
308.15	30000.00	0.0007
308.15	35000.00	0.0007
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	0.0008
318.15	10000.00	0.0008
318.15	15000.00	0.0008
318.15	20000.00	0.0008
318.15	25000.00	0.0008
318.15	30000.00	0.0007
318.15	35000.00	0.0007
318.15	40000.00	0.0007
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	0.0008
328.15	15000.00	0.0008
328.15	20000.00	0.0008
328.15	25000.00	0.0008
328.15	30000.00	0.0008
328.15	35000.00	0.0007
328.15	40000.00	0.0007
328.15	45000.00	0.0007
328.15	50000.00	0.0007
328.15	55000.00	0.0007
338.15	5000.00	0.0009
338.15	10000.00	0.0009
338.15	15000.00	0.0008
338.15	20000.00	0.0008
338.15	25000.00	0.0008
338.15	30000.00	0.0008
338.15	35000.00	0.0008
338.15	40000.00	0.0007
338.15	45000.00	0.0007
338.15	50000.00	0.0007
338.15	55000.00	0.0007
348.15	5000.00	0.0009
348.15	10000.00	0.0009
348.15	15000.00	0.0009
348.15	20000.00	0.0008
348.15	25000.00	0.0008
348.15	30000.00	0.0008
348.15	35000.00	0.0008
348.15	40000.00	0.0007
348.15	45000.00	0.0007
348.15	50000.00	0.0007
348.15	55000.00	0.0007
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	824.0
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
278.15	100.00	836.9
278.15	1000.00	837.4
278.15	5000.00	839.7
278.15	10000.00	842.5
278.15	15000.00	845.1
278.15	20000.00	847.8
278.15	25000.00	850.3
278.15	30000.00	852.8
278.15	35000.00	855.3
278.15	40000.00	857.6
278.15	45000.00	859.9
278.15	50000.00	862.2
278.15	55000.00	864.4
278.15	60000.00	866.4
288.15	100.00	829.9
288.15	1000.00	830.5
288.15	5000.00	832.7
288.15	10000.00	835.9
288.15	15000.00	838.7
288.15	20000.00	841.4
288.15	25000.00	844.0
288.15	30000.00	846.6
288.15	35000.00	849.1
288.15	40000.00	851.6
288.15	45000.00	854.0
288.15	50000.00	856.3
288.15	55000.00	858.6
288.15	60000.00	860.7
298.15	100.00	823.2
298.15	1000.00	823.7
298.15	5000.00	826.3
298.15	10000.00	829.4
298.15	15000.00	832.3
298.15	20000.00	835.1
298.15	25000.00	837.9
298.15	30000.00	840.5
298.15	35000.00	843.1
298.15	40000.00	845.7
298.15	45000.00	848.1
298.15	50000.00	850.5
298.15	55000.00	852.9
298.15	60000.00	855.0
308.15	100.00	816.5
308.15	1000.00	817.1
308.15	5000.00	819.8
308.15	10000.00	822.9
308.15	15000.00	826.0
308.15	20000.00	828.9
308.15	25000.00	831.8
308.15	30000.00	834.5
308.15	35000.00	837.2
308.15	40000.00	839.8
308.15	45000.00	842.4
308.15	50000.00	844.8
308.15	55000.00	847.3
308.15	60000.00	849.3
318.15	100.00	809.8
318.15	1000.00	810.4
318.15	5000.00	813.2
318.15	10000.00	816.5
318.15	15000.00	819.7
318.15	20000.00	822.7
318.15	25000.00	825.6
318.15	30000.00	828.5
318.15	35000.00	831.3
318.15	40000.00	834.0
318.15	45000.00	836.6
318.15	50000.00	839.2
318.15	55000.00	841.7
318.15	60000.00	844.0
328.15	100.00	802.8
328.15	1000.00	803.4
328.15	5000.00	806.3
328.15	10000.00	809.8
328.15	15000.00	813.1
328.15	20000.00	816.3
328.15	25000.00	819.3
328.15	30000.00	822.3
328.15	35000.00	825.2
328.15	40000.00	828.0
328.15	45000.00	830.7
328.15	50000.00	833.4
328.15	55000.00	836.0
328.15	60000.00	838.3
338.15	100.00	795.7
338.15	1000.00	796.4
338.15	5000.00	799.4
338.15	10000.00	803.0
338.15	15000.00	806.5
338.15	20000.00	809.8
338.15	25000.00	813.0
338.15	30000.00	816.1
338.15	35000.00	819.1
338.15	40000.00	822.0
338.15	45000.00	824.8
338.15	50000.00	827.6
338.15	55000.00	830.2
338.15	60000.00	832.7
348.15	100.00	788.3
348.15	1000.00	788.9
348.15	5000.00	792.3
348.15	10000.00	796.1
348.15	15000.00	799.7
348.15	20000.00	803.2
348.15	25000.00	806.6
348.15	30000.00	809.8
348.15	35000.00	812.9
348.15	40000.00	815.9
348.15	45000.00	818.8
348.15	50000.00	821.6
348.15	55000.00	824.4
348.15	60000.00	826.7
358.15	100.00	780.9
358.15	1000.00	781.6
358.15	5000.00	785.0
358.15	10000.00	789.0
358.15	15000.00	792.9
358.15	20000.00	796.5
358.15	25000.00	799.9
358.15	30000.00	803.3
358.15	35000.00	806.6
358.15	40000.00	809.7
358.15	45000.00	812.8
358.15	50000.00	815.7
358.15	55000.00	818.6
358.15	60000.00	821.2
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	1990.00	825.5
298.15	3990.00	826.7
298.15	6000.00	828.0
298.15	8010.00	829.2
298.15	10010.00	830.5
298.15	13000.00	832.2
298.15	16000.00	833.9
298.15	19010.00	835.5
298.15	21990.00	837.1
298.15	25000.00	838.7
298.15	28020.00	840.2
298.15	30020.00	841.1
303.15	2010.00	822.0
303.15	4010.00	823.2
303.15	6020.00	824.5
303.15	8030.00	825.7
303.15	9990.00	826.9
303.15	12980.00	828.7
303.15	15970.00	830.4
303.15	19020.00	832.1
303.15	22010.00	833.8
303.15	25000.00	835.4
303.14	27980.00	836.9
303.15	30000.00	837.9
313.15	2000.00	814.9
313.15	3970.00	816.3
313.15	6020.00	817.6
313.15	7990.00	818.9
313.15	10020.00	820.2
313.15	13000.00	822.0
313.15	16000.00	823.8
313.15	18980.00	825.6
313.15	22000.00	827.3
313.15	25000.00	829.0
313.15	28010.00	830.6
313.15	29990.00	831.7
323.15	2010.00	808.3
323.15	4020.00	809.7
323.15	6020.00	811.0
323.15	8010.00	812.3
323.15	10010.00	813.7
323.15	13010.00	815.7
323.15	16010.00	817.5
323.15	19000.00	819.3
323.15	22010.00	821.1
323.15	25000.00	822.9
323.15	28000.00	824.6
323.15	30000.00	825.7
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	824.0
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[220.92; 566.06]	J/mol×K	[298.15; 1500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + B·((C/T)/sinh(C/T))² + D·((E/T)/cosh(E/T))² Y is Cp,gas in J/mol×K, T in K
Coefficient A			1.54000e+02
Coefficient B			4.93600e+02
Coefficient C			1.57800e+03
Coefficient D			3.58800e+02
Coefficient E			7.21110e+02
Temperature range, min.			298.15
Temperature range, max.			1500.00
Cp,gas	220.92	J/mol×K	298.15	Calculated Property
Cp,gas	303.91	J/mol×K	431.69	Calculated Property
Cp,gas	369.01	J/mol×K	565.23	Calculated Property
Cp,gas	419.25	J/mol×K	698.77	Calculated Property
Cp,gas	459.07	J/mol×K	832.31	Calculated Property
Cp,gas	490.84	J/mol×K	965.84	Calculated Property
Cp,gas	516.21	J/mol×K	1099.38	Calculated Property
Cp,gas	536.51	J/mol×K	1232.92	Calculated Property
Cp,gas	552.83	J/mol×K	1366.46	Calculated Property
Cp,gas	566.06	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[350.59; 464.94]	J/mol×K	[310.00; 460.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,liquid in J/mol×K, T in K
Coefficient A			1.04830e+04
Coefficient B			-1.15220e+02
Coefficient C			4.76870e-01
Coefficient D			-8.53810e-04
Coefficient E			5.62460e-07
Temperature range, min.			310.00
Temperature range, max.			460.00
Cp,liquid	350.59	J/mol×K	310.00	Calculated Property
Cp,liquid	373.74	J/mol×K	326.67	Calculated Property
Cp,liquid	397.13	J/mol×K	343.33	Calculated Property
Cp,liquid	417.96	J/mol×K	360.00	Calculated Property
Cp,liquid	434.51	J/mol×K	376.67	Calculated Property
Cp,liquid	446.07	J/mol×K	393.33	Calculated Property
Cp,liquid	452.98	J/mol×K	410.00	Calculated Property
Cp,liquid	456.64	J/mol×K	426.67	Calculated Property
Cp,liquid	459.47	J/mol×K	443.33	Calculated Property
Cp,liquid	464.94	J/mol×K	460.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0173328; 0.0002823]	Pa×s	[280.00; 486.25]	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			-3.98630e+01
Coefficient B			4.08900e+03
Coefficient C			3.76310e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			280.00
Temperature range, max.			486.25
η	0.0173328	Pa×s	280.00	Calculated Property
η	0.0077201	Pa×s	302.92	Calculated Property
η	0.0039309	Pa×s	325.83	Calculated Property
η	0.0022256	Pa×s	348.75	Calculated Property
η	0.0013724	Pa×s	371.67	Calculated Property
η	0.0009073	Pa×s	394.58	Calculated Property
η	0.0006353	Pa×s	417.50	Calculated Property
η	0.0004667	Pa×s	440.42	Calculated Property
η	0.0003568	Pa×s	463.33	Calculated Property
η	0.0002823	Pa×s	486.25	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[82.41; 0.00]	kJ/mol	[268.15; 670.90]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K
Coefficient A			7.54290e+01
Coefficient B			-1.59660e+00
Coefficient C			4.64890e+00
Coefficient D			-2.72290e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			6.70900e+02
Temperature range, min.			268.15
Temperature range, max.			670.90
ΔvapH	82.41	kJ/mol	268.15	Calculated Property
ΔvapH	76.42	kJ/mol	312.90	Calculated Property
ΔvapH	69.48	kJ/mol	357.65	Calculated Property
ΔvapH	62.11	kJ/mol	402.40	Calculated Property
ΔvapH	54.72	kJ/mol	447.15	Calculated Property
ΔvapH	47.62	kJ/mol	491.90	Calculated Property
ΔvapH	40.94	kJ/mol	536.65	Calculated Property
ΔvapH	34.57	kJ/mol	581.40	Calculated Property
ΔvapH	27.67	kJ/mol	626.15	Calculated Property
ΔvapH	0.00	kJ/mol	670.90	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.67]	kPa	[372.65; 513.02]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.43149e+01
Coefficient B			-3.52869e+03
Coefficient C			-1.21090e+02
Temperature range, min.			372.65
Temperature range, max.			513.02
Pvap	1.33	kPa	372.65	Calculated Property
Pvap	3.02	kPa	388.25	Calculated Property
Pvap	6.27	kPa	403.84	Calculated Property
Pvap	12.03	kPa	419.44	Calculated Property
Pvap	21.65	kPa	435.04	Calculated Property
Pvap	36.86	kPa	450.63	Calculated Property
Pvap	59.80	kPa	466.23	Calculated Property
Pvap	93.04	kPa	481.83	Calculated Property
Pvap	139.55	kPa	497.42	Calculated Property
Pvap	202.67	kPa	513.02	Calculated Property
Pvap	[8.55e-05; 2522.38]	kPa	[268.15; 670.90]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			1.55942e+02
Coefficient B			-1.52050e+04
Coefficient C			-1.94240e+01
Coefficient D			1.07220e-17
Coefficient E			6.00000e+00
Temperature range, min.			268.15
Temperature range, max.			670.90
Pvap	8.55e-05	kPa	268.15	Calculated Property
Pvap	0.01	kPa	312.90	Calculated Property
Pvap	0.47	kPa	357.65	Calculated Property
Pvap	5.52	kPa	402.40	Calculated Property
Pvap	32.49	kPa	447.15	Calculated Property
Pvap	120.07	kPa	491.90	Calculated Property
Pvap	323.31	kPa	536.65	Calculated Property
Pvap	707.46	kPa	581.40	Calculated Property
Pvap	1369.91	kPa	626.15	Calculated Property
Pvap	2522.38	kPa	670.90	Calculated Property
Pvap	[6.76e-05; 2672.04]	kPa	[268.15; 673.00]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			2.51000e+02
Coefficient B			-1.90455e+04
Coefficient C			-3.41120e+01
Coefficient D			1.61583e-05
Coefficient E			0.00000e+00
Temperature range, min.			268.15
Temperature range, max.			673.00
Pvap	6.76e-05	kPa	268.15	Calculated Property
Pvap	0.01	kPa	313.13	Calculated Property
Pvap	0.49	kPa	358.12	Calculated Property
Pvap	5.66	kPa	403.10	Calculated Property
Pvap	32.69	kPa	448.08	Calculated Property
Pvap	119.75	kPa	493.07	Calculated Property
Pvap	325.72	kPa	538.05	Calculated Property
Pvap	729.96	kPa	583.03	Calculated Property
Pvap	1447.73	kPa	628.02	Calculated Property
Pvap	2672.04	kPa	673.00	Calculated Property
Pvap	[0.75; 102.48]	kPa	[364.80; 486.80]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.37270e+01
Coefficient B			-3.16241e+03
Coefficient C			-1.39182e+02
Reference			Kemme and Kreps, 1969
Temperature range, min.			364.80
Temperature range, max.			486.80
Pvap	0.75	kPa	364.80	Calculated Property
Pvap	1.66	kPa	378.36	Calculated Property
Pvap	3.37	kPa	391.91	Calculated Property
Pvap	6.37	kPa	405.47	Calculated Property
Pvap	11.32	kPa	419.02	Calculated Property
Pvap	19.07	kPa	432.58	Calculated Property
Pvap	30.70	kPa	446.13	Calculated Property
Pvap	47.47	kPa	459.69	Calculated Property
Pvap	70.85	kPa	473.24	Calculated Property
Pvap	102.48	kPa	486.80	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[843.83; 250.44]	kg/m3	[268.15; 670.90]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			6.30135e+01
Coefficient B			2.51610e-01
Coefficient C			6.70900e+02
Coefficient D			2.49800e-01
Temperature range, min.			268.15
Temperature range, max.			670.90
ρl	843.83	kg/m3	268.15	Calculated Property
ρl	814.63	kg/m3	312.90	Calculated Property
ρl	783.71	kg/m3	357.65	Calculated Property
ρl	750.65	kg/m3	402.40	Calculated Property
ρl	714.85	kg/m3	447.15	Calculated Property
ρl	675.33	kg/m3	491.90	Calculated Property
ρl	630.44	kg/m3	536.65	Calculated Property
ρl	576.80	kg/m3	581.40	Calculated Property
ρl	505.15	kg/m3	626.15	Calculated Property
ρl	250.44	kg/m3	670.90	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.01]	N/m	[267.65; 488.15]	Jasper (1972), surface tension of pure liquid compounds Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K
Coefficient A			5.13415e-02
Coefficient B			-7.89000e-05
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			267.65
Temperature range, max.			488.15
γ	0.03	N/m	267.65	Calculated Property
γ	0.03	N/m	292.15	Calculated Property
γ	0.03	N/m	316.65	Calculated Property
γ	0.02	N/m	341.15	Calculated Property
γ	0.02	N/m	365.65	Calculated Property
γ	0.02	N/m	390.15	Calculated Property
γ	0.02	N/m	414.65	Calculated Property
γ	0.02	N/m	439.15	Calculated Property
γ	0.01	N/m	463.65	Calculated Property
γ	0.01	N/m	488.15	Calculated Property
γ	[0.03; 0.00]	N/m	[268.15; 670.90]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is γ in N/m, T in K
Coefficient A			5.17520e-02
Coefficient B			1.05620e+00
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Critical temperature, Tc (K)			6.70900e+02
Temperature range, min.			268.15
Temperature range, max.			670.90
γ	0.03	N/m	268.15	Calculated Property
γ	0.03	N/m	312.90	Calculated Property
γ	0.02	N/m	357.65	Calculated Property
γ	0.02	N/m	402.40	Calculated Property
γ	0.02	N/m	447.15	Calculated Property
γ	0.01	N/m	491.90	Calculated Property
γ	0.01	N/m	536.65	Calculated Property
γ	0.01	N/m	581.40	Calculated Property
γ	0.00	N/m	626.15	Calculated Property
γ	0.00	N/m	670.90	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.02; 0.10]	W/m×K	[485.20; 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			-3.07150e+01
Coefficient B			-1.07500e-01
Coefficient C			8.10700e+03
Coefficient D			-1.56830e+08
Temperature range, min.			485.20
Temperature range, max.			1000.00
λgas	0.02	W/m×K	485.20	Calculated Property
λgas	0.03	W/m×K	542.40	Calculated Property
λgas	0.04	W/m×K	599.60	Calculated Property
λgas	0.04	W/m×K	656.80	Calculated Property
λgas	0.05	W/m×K	714.00	Calculated Property
λgas	0.06	W/m×K	771.20	Calculated Property
λgas	0.07	W/m×K	828.40	Calculated Property
λgas	0.08	W/m×K	885.60	Calculated Property
λgas	0.09	W/m×K	942.80	Calculated Property
λgas	0.10	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.17; 0.10]	W/m×K	[268.15; 578.65]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is λliquid in W/m×K, T in K
Coefficient A			2.40540e-01
Coefficient B			-2.50000e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			268.15
Temperature range, max.			578.65
λliquid	0.17	W/m×K	268.15	Calculated Property
λliquid	0.16	W/m×K	302.65	Calculated Property
λliquid	0.16	W/m×K	337.15	Calculated Property
λliquid	0.15	W/m×K	371.65	Calculated Property
λliquid	0.14	W/m×K	406.15	Calculated Property
λliquid	0.13	W/m×K	440.65	Calculated Property
λliquid	0.12	W/m×K	475.15	Calculated Property
λliquid	0.11	W/m×K	509.65	Calculated Property
λliquid	0.10	W/m×K	544.15	Calculated Property
λliquid	0.10	W/m×K	578.65	Calculated Property

Similar Compounds

Find more compounds similar to 1-Nonanol.

Mixtures

• 1-Nonanol + Propanoic acid + Water
• Formamide, N,N-dimethyl- + 1-Nonanol
• 1-Nonanol + o-Xylene
• 1-Nonanol + Benzene, 1,3-dimethyl-
• p-Xylene + 1-Nonanol
• 1-Nonanol + Benzene, ethyl-
• 1-Nonanol + Mesitylene
• Propylene Glycol + 1-Nonanol
• 1,2-Ethanediol + 1-Nonanol
• 1-Nonanol + Cyclohexane
• Diosgenin + 1-Nonanol
• Estriol + 1-Nonanol
• 1-Nonanol + Cholesterol
• 1-Nonanol + Cholesterol + Cyclohexane
• Betulin + 1-Nonanol
• 1-Nonanol + 3-Hydroxyestra-1,3,5(10)-trien-17-one
• 1-Nonanol + 1-Hexanol
• 1-Nonanol + 1-Heptanol
• 1,3-Propanediol + 1-Nonanol
• Benzyl alcohol + 1-Nonanol

Find more mixtures with 1-Nonanol.

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.
• Cheméo Relay (1.0)
• ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
• Crippen Method
• Experimental solid-liquid phase equilibria of {cholesterol + binary solvent mixture: 1-Alcohol (C4-C10) + cyclohexane}
• Liquid-liquid phase equilibrium of (piperidinium-based ionic liquid + an alcohol) binary systems and modelling with NRHB and PCP-SAFT
• Unusual behavior of the isotope effect on miscibility of 1-hexyl-3-methylimidazolium bis(trifluorosulfonyl)imide with 1-alkanols
• Study of molecular interactions and preferential solvation in binary mixtures of cyclohexane and (C5-C10) 1-alkanol by Kirkwood-Buff integrals
• (Liquid + liquid) phase equilibria of 1-alkyl-3-methylimidazolium methylsulfate with alcohols, or ethers, or ketones
• (Liquid + liquid) equilibria of (water + propionic acid + alcohol) ternary systems
• (Liquid + liquid) equilibria of (water + lactic acid + alcohol) ternary systems
• Thermodynamic and transport properties of (1,2-ethanediol + 1-nonanol) at temperatures from (298.15 to 313.15) K
• Isobaric thermal expansivity behaviour against temperature and pressure of associating fluids
• Volumetric and ultrasonic behaviour of binary mixtures of 1-nonanol with o-cresol, m-cresol, p-cresol and anisole at T = (293.15 and 313.15) K
• Measurement and correlation of the excess molar enthalpy of (1-nonanol, or 1-decanol + acetonitrile) mixtures at (298.15, 303.15, and 308.15) K and atmospheric pressure
• PrhoT measurements and derived properties of liquid 1-alkanols
• Acoustic and thermodynamic properties of binary mixtures of 1-nonanol with o-xylene, m-xylene, p-xylene, ethylbenzene and mesitylene at T = (298.15 and 308.15) K
• Physico-chemical properties of binary mixtures of N,N-dimethylformamide with 1-octanol, 1-nonanol and 1-decanol at different temperatures
• 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
• Effect of temperature and chain length on the viscosity and surface tension of binary systems of N,N-dimethylformamide with 1-octanol, 1-nonanol and 1-decanol
• Experimental solubility for betulin and estrone in various solvents within the temperature range T = (293.2 to 328.2) K
• Experimental solubility of diosgenin and estriol in various solvents between T = (293.2-328.2) K
• Studies on the importance of chain length of alkanols on the thermodynamic and transport properties of liquid mixtures at various temperatures
• Influence of chlorine atom on interactions between halo-hydrocarbons and 1-nonanol: Density and speed of sound measurements
• 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)
• Effect of chain length of alcohol on thermodynamic properties of their binary mixtures with benzylalcohol
• Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
• Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
• Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
• Viscosity and Density of n-Alcohols at Temperatures between (298.15 and 323.15) K and Pressures up to 30 MPa
• 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
• Thermodynamic Properties of 1-Hexyl-3-methylimidazolium Nitrate and 1-Alkanols Mixtures: PC-SAFT Model
• Experimental Solid + Liquid Equilibria and Excess Molar Volume of Alkanol + Octylamine Mixtures. Analysis in Terms of ERAS, DISQUAC, and Modified UNIFAC
• 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
• Density and Relative Permittivity for 1-Alkanols + Dodecane at 298.15 K
• Measurement of Density and Viscosity of Binary 1-Alkanol Systems (C8-C11) at 101 kPa and Temperatures from (283.15 to 313.15) K
• Experimental (Solid + Liquid) and (Liquid + Liquid) Equilibria and Excess Molar Volume of Alkanol + Acetonitrile, Propanenitrile, and Butanenitrile Mixtures
• Distribution of Butyric Acid between Water and Several Solvents
• 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
• Speeds of Sound, Densities, Isobaric Thermal Expansion, Compressibilities, and Internal Pressures of Heptan-1-ol, Octan-1-ol, Nonan-1-ol, and Decan-1-ol at Temperatures from (293 to 318) K and Pressures up to 100 MPa
• Densities, Speeds of Sound, and Isentropic Compressibilities of Binary Mixtures of {Alkan-1-ols + 1,2-Dimethylbenzene, or 1,3-Dimethylbenzene, or 1,4-Dimethylbenzene, or Ethylbenzene} at (293.15, 303.15, and 313.15) K
• Liquid-Liquid Phase Behavior of Solutions of 1-Hexyl-3-methylimidazolium Bis((trifluoromethyl)sulfonyl)amide (C6mimNTf2) in n-Alkyl Alcohols
• Micellar Properties and Related Thermodynamic Parameters of Aqueous Anionic Surfactants in the Presence of Monohydric Alcohols
• Liquid Liquid Phase Equilibria of 1-Propanol + Water + n-Alcohol Ternary Systems at 298.15 K and Atmospheric Pressure
• Liquid Liquid Phase Behavior of Solutions of 1-Butyl-3-methylimidazolium Bis((trifluoromethyl)sulfonyl)amide (C4mimNTf2) in n-Alkyl Alcohols
• Density and Viscosity of the Binary Systems Ethanol + Butan-1-ol, + Pentan-1-ol, + Heptan-1-ol, + Octan-1-ol, Nonan-1-ol, + Decan-1-ol at 0.1 MPa and Temperatures from 283.15 K to 313.15 K
• Comparison Study on Temperature Dependence of the Interfacial Tension of n-Alkane Water and n-Alcohol Water Two Binary Systems
• Thermodynamics of Mixing Tetrahydrofuran with 1-Alkanols and Excess Enthalpies of Homomorphy-Related Systems
• Ternary Liquid-Liquid Equilibria of Acetonitrile and Water with Heptanoic Acid and Nonanol at 323.15 K and 1 atm
• Densities and Kinematic Viscosities of Ten Binary 1-Alkanol Liquid Systems at Temperatures of (293.15 and 298.15) K
• Densities, Speeds of Sound, and Isentropic Compressibilities for Binary Mixtures of 2-Ethyl-1-hexanol with 1-Pentanol, 1-Heptanol, or 1-Nonanol at the Temperature 298.15 K
• Liquid-Liquid Phase Behavior of Solutions of 1-Octyl- and 1-Decyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide (C8,10mimNTf2) in n-Alkyl Alcohols
• Density and Viscosity of Binary Mixtures of {1-Butyl-3-methylimidazolium Thiocyanate + 1-Heptanol, 1-Octanol, 1-Nonanol, or 1-Decanol}
• Densities, Speeds of Sound, and Isentropic Compressibilities for Binary Mixtures of 1,2-Ethanediol with 2-Ethyl-1-hexanol, 1-Heptanol, or Ethanol at the Temperature 298.15 K and Densities for Mixtures of 1,2-Ethanediol with 1-Nonanol at the Temperatures (293.15 and 298.15) K
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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