Chemical Properties of 1-Hexanol, 2-ethyl- (CAS 104-76-7)

InChI

InChI=1S/C8H18O/c1-3-5-6-8(4-2)7-9/h8-9H,3-7H2,1-2H3

InChI Key

YIWUKEYIRIRTPP-UHFFFAOYSA-N

Formula

C8H18O

SMILES

CCCCC(CC)CO

Molecular Weight¹

130.23

CAS

104-76-7

Other Names

• 2-EH
• 2-Ethyl-1-hexyl alcohol
• 2-Ethyl-hexanol-1
• 2-Ethylhexan-1-ol
• 2-Ethylhexanol
• 2-Ethylhexyl alcohol
• 2-ethyl-1-hexanol
• Ethyl-1-hexanol,2-
• Ethylhexanol
• Ethylhexyl alcohol
• Hexan-1-ol, 2-ethyl
• Hexanol, 2-ethyl-
• NSC 9300
• OCTYL ALCOHOL

• ω : Acentric Factor.
• 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).
• 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_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I_p : Polar retention indices.
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• c_sound,fluid : Speed of sound in fluid (m/s).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• V_c : Critical Volume (m³/kmol).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.5518		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ΔcH°liquid	-5287.78 ± 0.79	kJ/mol	NIST
μ	1.80	debye	KDB
ΔfG°	-122.78	kJ/mol	Joback Calculated Property
ΔfH°gas	[-367.50; -365.50]	kJ/mol
ΔfH°gas	-365.50	kJ/mol	KDB
ΔfH°gas	-367.50 ± 2.20	kJ/mol	NIST
ΔfH°liquid	-432.88 ± 0.79	kJ/mol	NIST
ΔfusH°	17.04	kJ/mol	Joback Calculated Property
ΔvapH°	68.50 ± 0.20	kJ/mol	NIST
IE	9.71	eV	Relay (1.0) Calculated Property
log10WS	[-2.11; -2.11]
log10WS	-2.11		Aq. Solubility Prediction
log10WS	-2.11		Estimated Solubility
logPoct/wat	2.195		Crippen Calculated Property
McVol	129.450	ml/mol	McGowan Calculated Property
NFPA Fire	2		KDB
NFPA Health	2		KDB
Pc	[2796.57; 2800.00]	kPa
Pc	2800.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Pc	2796.57	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	2800.00	kPa	KDB
Pc	2800.00 ± 100.00	kPa	NIST
Pc	2800.00 ± 200.00	kPa	NIST
Inp	[164.40; 1064.00]
Inp	992.00		NIST
Inp	1002.00		NIST
Inp	1019.00		NIST
Inp	1015.00		NIST
Inp	1017.00		NIST
Inp	986.00		NIST
Inp	990.00		NIST
Inp	1029.00		NIST
Inp	1029.00		NIST
Inp	1029.00		NIST
Inp	1030.00		NIST
Inp	1010.70		NIST
Inp	1010.70		NIST
Inp	1026.30		NIST
Inp	1029.00		NIST
Inp	1045.00		NIST
Inp	1015.20		NIST
Inp	1016.90		NIST
Inp	1037.00		NIST
Inp	1037.00		NIST
Inp	1014.90		NIST
Inp	1019.00		NIST
Inp	1038.00		NIST
Inp	1025.00		NIST
Inp	1030.00		NIST
Inp	1030.00		NIST
Inp	1020.00		NIST
Inp	1020.00		NIST
Inp	1028.00		NIST
Inp	1028.00		NIST
Inp	1049.00		NIST
Inp	1038.00		NIST
Inp	1038.00		NIST
Inp	1028.00		NIST
Inp	1031.00		NIST
Inp	1030.00		NIST
Inp	1040.00		NIST
Inp	1013.00		NIST
Inp	1019.00		NIST
Inp	1019.00		NIST
Inp	1016.00		NIST
Inp	1031.00		NIST
Inp	1029.00		NIST
Inp	1031.00		NIST
Inp	1034.00		NIST
Inp	1033.00		NIST
Inp	1027.00		NIST
Inp	1018.00		NIST
Inp	1035.00		NIST
Inp	1027.00		NIST
Inp	1025.00		NIST
Inp	1025.00		NIST
Inp	1035.00		NIST
Inp	1032.00		NIST
Inp	1031.00		NIST
Inp	1060.00		NIST
Inp	1032.00		NIST
Inp	1034.00		NIST
Inp	980.00		NIST
Inp	1030.00		NIST
Inp	1033.00		NIST
Inp	1034.00		NIST
Inp	1032.00		NIST
Inp	1033.00		NIST
Inp	1026.00		NIST
Inp	1028.00		NIST
Inp	1043.00		NIST
Inp	1024.00		NIST
Inp	1026.00		NIST
Inp	1031.00		NIST
Inp	998.00		NIST
Inp	1014.00		NIST
Inp	1042.00		NIST
Inp	1016.10		NIST
Inp	1015.00		NIST
Inp	1038.00		NIST
Inp	1012.00		NIST
Inp	1034.00		NIST
Inp	1028.00		NIST
Inp	1033.00		NIST
Inp	1030.00		NIST
Inp	1030.00		NIST
Inp	1012.00		NIST
Inp	1012.00		NIST
Inp	1015.00		NIST
Inp	1018.00		NIST
Inp	1016.00		NIST
Inp	1064.00		NIST
Inp	1013.00		NIST
Inp	1030.00		NIST
Inp	1030.00		NIST
Inp	1030.00		NIST
Inp	1035.00		NIST
Inp	1020.00		NIST
Inp	1040.00		NIST
Inp	1020.00		NIST
Inp	1039.00		NIST
Inp	1031.00		NIST
Inp	1032.00		NIST
Inp	1015.00		NIST
Inp	1031.00		NIST
Inp	1008.00		NIST
Inp	1019.00		NIST
Inp	1031.00		NIST
Inp	1028.00		NIST
Inp	1019.00		NIST
Inp	1031.00		NIST
Inp	1019.00		NIST
Inp	1015.00		NIST
Inp	1048.00		NIST
Inp	1043.00		NIST
Inp	1030.00		NIST
Inp	1030.00		NIST
Inp	1028.00		NIST
Inp	1028.00		NIST
Inp	1013.00		NIST
Inp	1029.00		NIST
Inp	1020.00		NIST
Inp	1034.00		NIST
Inp	1038.00		NIST
Inp	1033.00		NIST
Inp	1020.00		NIST
Inp	1015.00		NIST
Inp	1015.00		NIST
Inp	1014.00		NIST
Inp	1018.00		NIST
Inp	1018.00		NIST
Inp	1037.00		NIST
Inp	Outlier 164.40		NIST
Inp	1031.00		NIST
Inp	1027.00		NIST
Inp	1025.00		NIST
Inp	1032.00		NIST
Inp	1034.00		NIST
Inp	1043.00		NIST
Inp	1014.00		NIST
Inp	1012.00		NIST
Inp	1030.00		NIST
Inp	1016.00		NIST
Inp	1028.00		NIST
Inp	1040.00		NIST
Inp	1015.00		NIST
Inp	1048.00		NIST
Inp	1038.00		NIST
Inp	1019.00		NIST
Ip	[1441.00; 1522.00]
Ip	1484.00		NIST
Ip	1484.00		NIST
Ip	1484.00		NIST
Ip	1488.00		NIST
Ip	1499.00		NIST
Ip	1484.00		NIST
Ip	1480.00		NIST
Ip	1496.00		NIST
Ip	1470.00		NIST
Ip	1481.00		NIST
Ip	Outlier 1441.00		NIST
Ip	1484.00		NIST
Ip	1505.00		NIST
Ip	1517.00		NIST
Ip	1491.00		NIST
Ip	Outlier 1453.00		NIST
Ip	1484.00		NIST
Ip	Outlier 1446.00		NIST
Ip	1491.00		NIST
Ip	1479.00		NIST
Ip	1491.00		NIST
Ip	1474.00		NIST
Ip	1492.00		NIST
Ip	Outlier 1522.00		NIST
Ip	1494.00		NIST
Ip	1493.00		NIST
Ip	1502.00		NIST
Ip	1490.00		NIST
Ip	1493.00		NIST
Ip	Outlier 1444.00		NIST
Ip	1495.00		NIST
Ip	1473.00		NIST
Ip	1491.00		NIST
Ip	1491.00		NIST
Ip	1494.00		NIST
Ip	1489.00		NIST
Ip	1491.00		NIST
Ip	Outlier 1449.00		NIST
Ip	1493.00		NIST
Ip	1492.00		NIST
Ip	1492.00		NIST
Ip	1496.00		NIST
Ip	1483.00		NIST
Ip	1492.00		NIST
Ip	1488.00		NIST
Ip	1518.00		NIST
Ip	1504.00		NIST
Ip	1488.00		NIST
Ip	1490.00		NIST
Ip	1490.00		NIST
Ip	1481.00		NIST
Ip	1474.00		NIST
Ip	1518.00		NIST
Ip	1490.00		NIST
Ip	1489.00		NIST
Ip	Outlier 1450.00		NIST
Ip	1502.00		NIST
Ip	1503.00		NIST
Ip	1503.00		NIST
Ip	1490.00		NIST
Ip	1486.00		NIST
Ip	1483.00		NIST
Ip	1462.00		NIST
Ip	1488.00		NIST
Ip	1503.00		NIST
Ip	1484.00		NIST
Ip	1501.00		NIST
Ip	1494.00		NIST
Ip	1474.00		NIST
Ip	1495.00		NIST
Ip	1472.00		NIST
Ip	1515.00		NIST
Ip	1505.00		NIST
Ip	1476.00		NIST
Ip	1476.00		NIST
Ip	1512.00		NIST
Ip	1499.00		NIST
Ip	1484.00		NIST
Ip	1490.00		NIST
Ip	1487.00		NIST
Ip	1495.00		NIST
Ip	1484.00		NIST
Ip	1495.00		NIST
Ip	1496.00		NIST
Ip	1503.00		NIST
Ip	1503.00		NIST
Ip	1502.00		NIST
Ip	1491.00		NIST
Ip	1493.00		NIST
Ip	1509.00		NIST
Ip	1481.00		NIST
Ip	1475.00		NIST
Ip	1509.00		NIST
Ip	1492.00		NIST
Ip	1490.00		NIST
Ip	1492.00		NIST
Ip	Outlier 1458.00		NIST
Ip	1495.00		NIST
Ip	1490.00		NIST
Ip	1505.00		NIST
Ip	1491.00		NIST
Ip	1483.00		NIST
Ip	1461.00		NIST
Ip	1487.00		NIST
Ip	1491.00		NIST
Ip	Outlier 1453.00		NIST
Ip	Outlier 1453.00		NIST
Ip	Outlier 1453.00		NIST
Ip	1491.00		NIST
Ip	1515.00		NIST
Ip	Outlier 1520.00		NIST
Ip	1483.00		NIST
Ip	1491.00		NIST
Ip	1496.00		NIST
Ip	1495.00		NIST
Ip	1492.00		NIST
Ip	1502.00		NIST
Ip	1496.00		NIST
Ip	1504.00		NIST
Ip	1492.00		NIST
Ip	1493.00		NIST
Ip	1494.00		NIST
Ip	1485.00		NIST
Ip	1489.00		NIST
Ip	1491.00		NIST
Ip	1489.00		NIST
Ip	1492.00		NIST
Ip	1492.00		NIST
Ip	1489.00		NIST
Ip	1486.00		NIST
Ip	1495.00		NIST
Ip	1494.00		NIST
Ip	1493.00		NIST
Ip	1489.00		NIST
Ip	1496.00		NIST
Ip	1496.00		NIST
Ip	1496.00		NIST
Ip	1496.00		NIST
Ip	1496.00		NIST
Ip	1480.00		NIST
Ip	1495.00		NIST
Ip	1518.00		NIST
Ip	1476.00		NIST
Ip	1481.00		NIST
Ip	1482.00		NIST
Ip	1470.00		NIST
Ip	1492.00		NIST
Ip	1465.00		NIST
Ip	1502.00		NIST
Ip	1483.00		NIST
Ip	1501.00		NIST
Ip	1515.00		NIST
Ip	1499.00		NIST
Ip	1484.00		NIST
Ip	1475.00		NIST
Ip	Outlier 1458.00		NIST
Ip	Outlier 1453.00		NIST
Ip	1492.00		NIST
Ip	1488.00		NIST
Ip	1490.00		NIST
Ip	1489.00		NIST
S°liquid	347.00	J/mol×K	NIST
Tboil	[449.65; 458.20]	K
Tboil	458.20	K	(Liquid + liquid) equilibria of (water + propionic acid + 2-ethyl-1-hexanol): Experimental data and correlation
Tboil	457.77	K	KDB
Tboil	457.70	K	NIST
Tboil	457.45	K	NIST
Tboil	457.15 ± 3.00	K	NIST
Tboil	457.49 ± 0.50	K	NIST
Tboil	456.15 ± 3.00	K	NIST
Tboil	456.15 ± 3.00	K	NIST
Tboil	Outlier 449.65 ± 3.00	K	NIST
Tboil	457.95	K	NIST
Tboil	454.90 ± 3.00	K	NIST
Tboil	456.65 ± 3.00	K	NIST
Tboil	456.15 ± 3.00	K	NIST
Tboil	454.15 ± 3.00	K	NIST
Tboil	453.65 ± 3.00	K	NIST
Tboil	454.65 ± 3.00	K	NIST
Tboil	455.15 ± 3.00	K	NIST
Tboil	454.15 ± 3.00	K	NIST
Tboil	454.80 ± 3.00	K	NIST
Tboil	457.00 ± 3.00	K	NIST
Tboil	457.80 ± 1.00	K	NIST
Tboil	453.65 ± 3.00	K	NIST
Tboil	457.75 ± 2.00	K	NIST
Tboil	453.15 ± 3.00	K	NIST
Tboil	455.65 ± 5.00	K	NIST
Tc	[640.20; 641.00]	K
Tc	640.60	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Tc	640.80	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	640.60	K	KDB
Tc	641.00 ± 1.00	K	NIST
Tc	641.00 ± 2.00	K	NIST
Tc	640.20 ± 0.30	K	NIST
Tfus	[200.15; 203.00]	K
Tfus	200.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	203.00	K	KDB
Vc	0.494	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	317.50	J/mol×K	298.15	NIST
ΔvapH	[52.70; 60.20]	kJ/mol	[385.50; 402.00]
ΔvapH	52.70	kJ/mol	385.50	NIST
ΔvapH	60.20	kJ/mol	402.00	NIST
Pvap	[0.02; 103.26]	kPa	[293.80; 458.24]
Pvap	0.02	kPa	293.80	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	298.70	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	301.60	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	304.50	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	307.40	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	0.07	kPa	310.30	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	0.09	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	0.11	kPa	316.30	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	0.14	kPa	319.20	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	322.20	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	0.22	kPa	325.20	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	0.28	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	0.34	kPa	331.20	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	9.88	kPa	389.76	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	19.88	kPa	407.11	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	30.03	kPa	418.24	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	39.67	kPa	426.95	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	40.00	kPa	427.20	Isobaric Vapor Liquid Equilibria for Binary Systems Comprising 1-Chloro-2-ethylhexane, 2-Ethyl-1-hexanol, p-Xylene, and N-Methylpyrrolidone (NMP) at 40.0 kPa
Pvap	45.05	kPa	430.79	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	49.22	kPa	433.51	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	55.52	kPa	437.24	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	59.61	kPa	439.49	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	64.64	kPa	442.12	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	70.55	kPa	445.00	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	75.01	kPa	447.04	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	79.55	kPa	449.02	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	84.49	kPa	451.06	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	99.44	kPa	456.77	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	102.20	kPa	457.83	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	102.91	kPa	458.23	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap	103.26	kPa	458.24	Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
n0	[1.42130; 1.43160]		[293.10; 318.20]
n0	1.43100		293.10	Phase Equilibria of Binary Systems Comprising Formic Acid, N,N-Dimethylformamide, 1-Chloro-2-ethylhexane, and 2-Ethyl-1-hexanol
n0	1.43100		293.10	Vapor-Liquid Equilibria of Binary Systems Comprising 1-Chloro-2-ethylhexane and 2-Ethyl-1-hexanol
n0	1.42920		298.15	Acoustic and Thermodynamic Properties of 2-Ethyl-1-hexanol by Means of High-Pressure Speed of Sound Measurements at Temperatures from (293 to 318) K and Pressures up to 101 MPa
n0	1.42930		298.20	Solubility and tie line data for the aqueous solutions of butyric acid with 1-octanol and 2-ethyl-1-hexanol at various temperatures
n0	1.43160		298.20	Dielectric study of molecular association in the binary mixtures (2-ethyl-1-hexanol + alcohol) and (cyclohexane + alcohol) at 298.2 K
n0	1.42930		298.20	Dielectric properties of binary mixtures of three butanediols with 1,4-dioxane and 2-ethyl-1-hexanol at T = 298.2 K
n0	1.42930		298.20	Dielectric data of binary mixtures of 1,2-butanediol with 2-ethyl-1-hexanol and 1,4-dioxane at T = (298.2, 308.2, and 318.2) K
n0	1.42930		298.20	Tie-line data for the aqueous solutions of phenol with organic solvents at T = 298.2 K
n0	1.42520		308.20	Dielectric data of binary mixtures of 1,2-butanediol with 2-ethyl-1-hexanol and 1,4-dioxane at T = (298.2, 308.2, and 318.2) K
n0	1.42130		318.20	Dielectric data of binary mixtures of 1,2-butanediol with 2-ethyl-1-hexanol and 1,4-dioxane at T = (298.2, 308.2, and 318.2) K
ρl	[821.68; 833.00]	kg/m3	[293.00; 308.15]
ρl	833.00	kg/m3	293.00	KDB
ρl	829.07	kg/m3	298.15	Densities, Viscosities, Speeds of Sound, and Refractive Indices of Binary Mixtures of 2-Ethyl-1-hexanol with Benzene and Halobenzenes
ρl	825.39	kg/m3	303.15	Densities, Viscosities, Speeds of Sound, and Refractive Indices of Binary Mixtures of 2-Ethyl-1-hexanol with Benzene and Halobenzenes
ρl	821.68	kg/m3	308.15	Densities, Viscosities, Speeds of Sound, and Refractive Indices of Binary Mixtures of 2-Ethyl-1-hexanol with Benzene and Halobenzenes
csound,fluid	[1318.07; 1318.44]	m/s	[298.15; 298.15]
csound,fluid	1318.07	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	1318.44	m/s	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

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[187.38; 451.27]	J/mol×K	[273.00; 1000.00]	Joback Predicted correlation
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K
Coefficient A			-7.75000e-01
Coefficient B			8.03740e-01
Coefficient C			-4.45000e-04
Coefficient D			9.33000e-08
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	187.38	J/mol×K	273.00	Calculated Property
Cp,gas	232.01	J/mol×K	353.78	Calculated Property
Cp,gas	272.12	J/mol×K	434.56	Calculated Property
Cp,gas	308.01	J/mol×K	515.33	Calculated Property
Cp,gas	339.98	J/mol×K	596.11	Calculated Property
Cp,gas	368.31	J/mol×K	676.89	Calculated Property
Cp,gas	393.32	J/mol×K	757.67	Calculated Property
Cp,gas	415.28	J/mol×K	838.44	Calculated Property
Cp,gas	434.50	J/mol×K	919.22	Calculated Property
Cp,gas	451.27	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.5271584; 0.0002375]	Pa×s	[201.57; 448.49]	Joback Predicted correlation
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-1.46357e+01
Coefficient B			2.82113e+03
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Comment			Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc.
Temperature range, min.			201.57
Temperature range, max.			448.49
η	0.5271584	Pa×s	201.57	Calculated Property
η	0.0985804	Pa×s	229.01	Calculated Property
η	0.0263899	Pa×s	256.44	Calculated Property
η	0.0091141	Pa×s	283.88	Calculated Property
η	0.0037964	Pa×s	311.31	Calculated Property
η	0.0018223	Pa×s	338.75	Calculated Property
η	0.0009765	Pa×s	366.18	Calculated Property
η	0.0005708	Pa×s	393.62	Calculated Property
η	0.0003578	Pa×s	421.05	Calculated Property
η	0.0002375	Pa×s	448.49	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[349.00; 482.60]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.43882e+01
Coefficient B			-3.40352e+03
Coefficient C			-1.07630e+02
Temperature range, min.			349.00
Temperature range, max.			482.60
Pvap	1.33	kPa	349.00	Calculated Property
Pvap	3.02	kPa	363.84	Calculated Property
Pvap	6.25	kPa	378.69	Calculated Property
Pvap	11.99	kPa	393.53	Calculated Property
Pvap	21.57	kPa	408.38	Calculated Property
Pvap	36.73	kPa	423.22	Calculated Property
Pvap	59.63	kPa	438.07	Calculated Property
Pvap	92.85	kPa	452.91	Calculated Property
Pvap	139.39	kPa	467.76	Calculated Property
Pvap	202.63	kPa	482.60	Calculated Property
Pvap	[7.91e-10; 2836.74]	kPa	[203.15; 640.25]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			3.04517e+02
Coefficient B			-2.04556e+04
Coefficient C			-4.24888e+01
Coefficient D			2.42482e-05
Coefficient E			0.00000e+00
Temperature range, min.			203.15
Temperature range, max.			640.25
Pvap	7.91e-10	kPa	203.15	Calculated Property
Pvap	4.10e-05	kPa	251.72	Calculated Property
Pvap	0.02	kPa	300.28	Calculated Property
Pvap	1.08	kPa	348.85	Calculated Property
Pvap	13.20	kPa	397.42	Calculated Property
Pvap	72.22	kPa	445.98	Calculated Property
Pvap	244.60	kPa	494.55	Calculated Property
Pvap	626.49	kPa	543.12	Calculated Property
Pvap	1378.79	kPa	591.68	Calculated Property
Pvap	2836.74	kPa	640.25	Calculated Property
Pvap	[1.00; 99.11]	kPa	[347.22; 456.70]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.38475e+01
Coefficient B			-3.05311e+03
Coefficient C			-1.26680e+02
Reference			Dykyj, Seprakova, et al., 1961
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			347.22
Temperature range, max.			456.70
Pvap	1.00	kPa	347.22	Calculated Property
Pvap	2.07	kPa	359.38	Calculated Property
Pvap	3.97	kPa	371.55	Calculated Property
Pvap	7.17	kPa	383.71	Calculated Property
Pvap	12.26	kPa	395.88	Calculated Property
Pvap	20.01	kPa	408.04	Calculated Property
Pvap	31.38	kPa	420.21	Calculated Property
Pvap	47.46	kPa	432.37	Calculated Property
Pvap	69.56	kPa	444.54	Calculated Property
Pvap	99.11	kPa	456.70	Calculated Property

Similar Compounds

Find more compounds similar to 1-Hexanol, 2-ethyl-.

Mixtures

• 1-Hexanol, 2-ethyl- + Phenol + Water
• 1-Hexanol, 2-ethyl- + Water
• 2,3-Butanediol + 1-Hexanol, 2-ethyl- + Water
• Carbon dioxide + Hexanoic acid, 2-ethyl- + 1-Hexanol, 2-ethyl-
• Acetic acid + 1-Hexanol, 2-ethyl- + Water
• 1-Hexanol, 2-ethyl- + Propanoic acid + Water
• Propylene Glycol + 1-Hexanol, 2-ethyl- + Water
• 1-Butanol + 1-Hexanol, 2-ethyl-
• 2-Propanol, 2-methyl- + 1-Hexanol, 2-ethyl-
• 2,3-Butanediol + 1-Hexanol, 2-ethyl-
• 1,4-Butanediol + 1-Hexanol, 2-ethyl-
• Butanoic acid + 1-Hexanol, 2-ethyl- + Water
• Ethanol + 1-Hexanol, 2-ethyl-
• Benzene + 1-Hexanol, 2-ethyl-
• Benzene, chloro- + 1-Hexanol, 2-ethyl-
• Benzene, bromo- + 1-Hexanol, 2-ethyl-
• Formic acid + 1-Hexanol, 2-ethyl-
• 1-Pentanol + 1-Hexanol, 2-ethyl-
• 1-Hexanol, 2-ethyl- + Water + 2-ethylhexyl thioglycolate
• 1,2-Ethanediol + 1-Hexanol, 2-ethyl-

Find more mixtures with 1-Hexanol, 2-ethyl-.

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.
• 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)
• Crippen Method
• Densities, Viscosities, Speeds of Sound, and Refractive Indices of Binary Mixtures of 2-Ethyl-1-hexanol with Benzene and Halobenzenes
• Isobaric vapor liquid phase equilibria for the binary systems of tert-butanol + 2-ethyl-1-hexanol and n-butanol + 2-ethyl-1-hexanol
• The co-solubility of 2-ethylhexanoic acid and some liquid alcohols in supercritical carbon dioxide
• Liquid liquid equilibria of (water + 2,3-butanediol + 2-ethyl-1-hexanol) at several temperatures
• Phase equilibria in ternary aqueous mixtures of 1,3-butanediol with 2-ethyl-1-hexanol at T = (298.2, 303.2 and 308.2) K
• Experimental and correlated tie-line data for aqueous mixtures of 2-butanol with 2-ethyl-1-hexanol at various temperatures
• Solubility and tie line data for the aqueous solutions of butyric acid with 1-octanol and 2-ethyl-1-hexanol at various temperatures
• Solubility and dissolution characteristics of capecitabine in pure lower alcohols and water with methanol mixture solvents at atmospheric pressure and different temperatures
• (Liquid + liquid) equilibria for (water + acetic acid + 2-ethyl- 1-hexanol): experimental data and prediction
• Dielectric study of molecular association in the binary mixtures (2-ethyl-1-hexanol + alcohol) and (cyclohexane + alcohol) at 298.2 K
• (Liquid + liquid) equilibria of (water + propionic acid + 2-ethyl-1-hexanol): Experimental data and correlation
• Dielectric properties of binary mixtures of three butanediols with 1,4-dioxane and 2-ethyl-1-hexanol at T = 298.2 K
• Dielectric data of binary mixtures of 1,2-butanediol with 2-ethyl-1-hexanol and 1,4-dioxane at T = (298.2, 308.2, and 318.2) K
• Phase diagrams for (water + 1, 2-butanediol or 1, 2-propanediol + 2-ethyl-1-hexanol) systems: Experimental data and UNIQUAC
• Tie-line data for the aqueous solutions of phenol with organic solvents at T = 298.2 K
• Measurement and Correlation of the Solubility of Florfenicol Form A in Several Pure and Binary Solvents
• Liquid-Liquid Equilibria for the Ternary Systems of Water + Thioglycolic Acid + 2-Ethyl-1-hexyl Thioglycolate and Water + 2-Ethyl-1-hexyl Thioglycolate + 2-Ethyl-1-hexanol at 293.15, 303.15, and 313.15 K under 101 kPa
• Liquid-Liquid Equilibria for the Ternary and Quaternary Systems of Water + Trimethylolpropane + (2-Ethylhexan-1-ol/Octan-1-ol) + Formaldehyde at 298.15 K
• Solubility of 2-Ethyl-1-hexanol, 2-Ethylhexanoic Acid, and Their Mixtures in Supercritical Carbon Dioxide
• Liquid-Liquid Equilibria of Water + 1-Butanol + 2-Ethyl-1-hexanol System
• 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
• Acoustic and Thermodynamic Properties of 2-Ethyl-1-hexanol by Means of High-Pressure Speed of Sound Measurements at Temperatures from (293 to 318) K and Pressures up to 101 MPa
• Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
• Isobaric Vapor Liquid Equilibria for Binary Systems Comprising 1-Chloro-2-ethylhexane, 2-Ethyl-1-hexanol, p-Xylene, and N-Methylpyrrolidone (NMP) at 40.0 kPa
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• Experimental Vapor Liquid Equilibria for the Systems {2-Ethyl-1-hexanol + Glycerol + CO2} and {2-Methyl-2-propanol + Glycerol + CO2}
• Phase Equilibria of Binary Systems Comprising Formic Acid, N,N-Dimethylformamide, 1-Chloro-2-ethylhexane, and 2-Ethyl-1-hexanol
• Vapor-Liquid Equilibria of Binary Systems Comprising 1-Chloro-2-ethylhexane and 2-Ethyl-1-hexanol
• Experimental and Theoretical Study of the Phase Equilibria in Ternary Aqueous Mixtures of 1,4-Butanediol with Alcohols at 298.2 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
• 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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