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

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Physical Properties

Property	Value	Unit	Source
ω	0.6336		Relay (1.0) Calculated Property
Δ_cH°_liquid	-5287.78 ± 0.79	kJ/mol	NIST
μ	1.80	debye	KDB
Δ_fG°	-122.78	kJ/mol	Joback Calculated Property
Δ_fH°_gas	[-367.50; -365.50]	kJ/mol
Δ_fH°_gas	-365.50	kJ/mol	KDB
Δ_fH°_gas	-367.50 ± 2.20	kJ/mol	NIST
Δ_fH°_liquid	-432.88 ± 0.79	kJ/mol	NIST
Δ_fusH°	17.04	kJ/mol	Joback Calculated Property
Δ_vapH°	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
logP_oct/wat	2.195		Crippen Calculated Property
McVol	129.450	ml/mol	McGowan Calculated Property
NFPA Fire	2		KDB
NFPA Health	2		KDB
P_c	[2800.00; 2800.00]	kPa
P_c	2800.00	kPa	KDB
P_c	2800.00 ± 100.00	kPa	NIST
P_c	2800.00 ± 200.00	kPa	NIST
I_np	[164.40; 1064.00]
I_np	992.00		NIST
I_np	1002.00		NIST
I_np	1019.00		NIST
I_np	1015.00		NIST
I_np	1017.00		NIST
I_np	986.00		NIST
I_np	990.00		NIST
I_np	1029.00		NIST
I_np	1029.00		NIST
I_np	1029.00		NIST
I_np	1030.00		NIST
I_np	1010.70		NIST
I_np	1010.70		NIST
I_np	1026.30		NIST
I_np	1029.00		NIST
I_np	1045.00		NIST
I_np	1015.20		NIST
I_np	1016.90		NIST
I_np	1037.00		NIST
I_np	1037.00		NIST
I_np	1014.90		NIST
I_np	1019.00		NIST
I_np	1038.00		NIST
I_np	1025.00		NIST
I_np	1030.00		NIST
I_np	1030.00		NIST
I_np	1020.00		NIST
I_np	1020.00		NIST
I_np	1028.00		NIST
I_np	1028.00		NIST
I_np	1049.00		NIST
I_np	1038.00		NIST
I_np	1038.00		NIST
I_np	1028.00		NIST
I_np	1031.00		NIST
I_np	1030.00		NIST
I_np	1040.00		NIST
I_np	1013.00		NIST
I_np	1019.00		NIST
I_np	1019.00		NIST
I_np	1016.00		NIST
I_np	1031.00		NIST
I_np	1029.00		NIST
I_np	1031.00		NIST
I_np	1034.00		NIST
I_np	1033.00		NIST
I_np	1027.00		NIST
I_np	1018.00		NIST
I_np	1035.00		NIST
I_np	1027.00		NIST
I_np	1025.00		NIST
I_np	1025.00		NIST
I_np	1035.00		NIST
I_np	1032.00		NIST
I_np	1031.00		NIST
I_np	1060.00		NIST
I_np	1032.00		NIST
I_np	1034.00		NIST
I_np	980.00		NIST
I_np	1030.00		NIST
I_np	1033.00		NIST
I_np	1034.00		NIST
I_np	1032.00		NIST
I_np	1033.00		NIST
I_np	1026.00		NIST
I_np	1028.00		NIST
I_np	1043.00		NIST
I_np	1024.00		NIST
I_np	1026.00		NIST
I_np	1031.00		NIST
I_np	998.00		NIST
I_np	1014.00		NIST
I_np	1042.00		NIST
I_np	1016.10		NIST
I_np	1015.00		NIST
I_np	1038.00		NIST
I_np	1012.00		NIST
I_np	1034.00		NIST
I_np	1028.00		NIST
I_np	1033.00		NIST
I_np	1030.00		NIST
I_np	1030.00		NIST
I_np	1012.00		NIST
I_np	1012.00		NIST
I_np	1015.00		NIST
I_np	1018.00		NIST
I_np	1016.00		NIST
I_np	1064.00		NIST
I_np	1013.00		NIST
I_np	1030.00		NIST
I_np	1030.00		NIST
I_np	1030.00		NIST
I_np	1035.00		NIST
I_np	1020.00		NIST
I_np	1040.00		NIST
I_np	1020.00		NIST
I_np	1039.00		NIST
I_np	1031.00		NIST
I_np	1032.00		NIST
I_np	1015.00		NIST
I_np	1031.00		NIST
I_np	1008.00		NIST
I_np	1019.00		NIST
I_np	1031.00		NIST
I_np	1028.00		NIST
I_np	1019.00		NIST
I_np	1031.00		NIST
I_np	1019.00		NIST
I_np	1015.00		NIST
I_np	1048.00		NIST
I_np	1043.00		NIST
I_np	1030.00		NIST
I_np	1030.00		NIST
I_np	1028.00		NIST
I_np	1028.00		NIST
I_np	1013.00		NIST
I_np	1029.00		NIST
I_np	1020.00		NIST
I_np	1034.00		NIST
I_np	1038.00		NIST
I_np	1033.00		NIST
I_np	1020.00		NIST
I_np	1015.00		NIST
I_np	1015.00		NIST
I_np	1014.00		NIST
I_np	1018.00		NIST
I_np	1018.00		NIST
I_np	1037.00		NIST
I_np	Outlier 164.40		NIST
I_np	1031.00		NIST
I_np	1027.00		NIST
I_np	1025.00		NIST
I_np	1032.00		NIST
I_np	1034.00		NIST
I_np	1043.00		NIST
I_np	1014.00		NIST
I_np	1012.00		NIST
I_np	1030.00		NIST
I_np	1016.00		NIST
I_np	1028.00		NIST
I_np	1040.00		NIST
I_np	1015.00		NIST
I_np	1048.00		NIST
I_np	1038.00		NIST
I_np	1019.00		NIST
I	[1441.00; 1522.00]
I	1484.00		NIST
I	1484.00		NIST
I	1484.00		NIST
I	1488.00		NIST
I	1499.00		NIST
I	1484.00		NIST
I	1480.00		NIST
I	1496.00		NIST
I	1470.00		NIST
I	1481.00		NIST
I	Outlier 1441.00		NIST
I	1484.00		NIST
I	1505.00		NIST
I	1517.00		NIST
I	1491.00		NIST
I	Outlier 1453.00		NIST
I	1484.00		NIST
I	Outlier 1446.00		NIST
I	1491.00		NIST
I	1479.00		NIST
I	1491.00		NIST
I	1474.00		NIST
I	1492.00		NIST
I	Outlier 1522.00		NIST
I	1494.00		NIST
I	1493.00		NIST
I	1502.00		NIST
I	1490.00		NIST
I	1493.00		NIST
I	Outlier 1444.00		NIST
I	1495.00		NIST
I	1473.00		NIST
I	1491.00		NIST
I	1491.00		NIST
I	1494.00		NIST
I	1489.00		NIST
I	1491.00		NIST
I	Outlier 1449.00		NIST
I	1493.00		NIST
I	1492.00		NIST
I	1492.00		NIST
I	1496.00		NIST
I	1483.00		NIST
I	1492.00		NIST
I	1488.00		NIST
I	1518.00		NIST
I	1504.00		NIST
I	1488.00		NIST
I	1490.00		NIST
I	1490.00		NIST
I	1481.00		NIST
I	1474.00		NIST
I	1518.00		NIST
I	1490.00		NIST
I	1489.00		NIST
I	Outlier 1450.00		NIST
I	1502.00		NIST
I	1503.00		NIST
I	1503.00		NIST
I	1490.00		NIST
I	1486.00		NIST
I	1483.00		NIST
I	1462.00		NIST
I	1488.00		NIST
I	1503.00		NIST
I	1484.00		NIST
I	1501.00		NIST
I	1494.00		NIST
I	1474.00		NIST
I	1495.00		NIST
I	1472.00		NIST
I	1515.00		NIST
I	1505.00		NIST
I	1476.00		NIST
I	1476.00		NIST
I	1512.00		NIST
I	1499.00		NIST
I	1484.00		NIST
I	1490.00		NIST
I	1487.00		NIST
I	1495.00		NIST
I	1484.00		NIST
I	1495.00		NIST
I	1496.00		NIST
I	1503.00		NIST
I	1503.00		NIST
I	1502.00		NIST
I	1491.00		NIST
I	1493.00		NIST
I	1509.00		NIST
I	1481.00		NIST
I	1475.00		NIST
I	1509.00		NIST
I	1492.00		NIST
I	1490.00		NIST
I	1492.00		NIST
I	Outlier 1458.00		NIST
I	1495.00		NIST
I	1490.00		NIST
I	1505.00		NIST
I	1491.00		NIST
I	1483.00		NIST
I	1461.00		NIST
I	1487.00		NIST
I	1491.00		NIST
I	Outlier 1453.00		NIST
I	Outlier 1453.00		NIST
I	Outlier 1453.00		NIST
I	1491.00		NIST
I	1515.00		NIST
I	Outlier 1520.00		NIST
I	1483.00		NIST
I	1491.00		NIST
I	1496.00		NIST
I	1495.00		NIST
I	1492.00		NIST
I	1502.00		NIST
I	1496.00		NIST
I	1504.00		NIST
I	1492.00		NIST
I	1493.00		NIST
I	1494.00		NIST
I	1485.00		NIST
I	1489.00		NIST
I	1491.00		NIST
I	1489.00		NIST
I	1492.00		NIST
I	1492.00		NIST
I	1489.00		NIST
I	1486.00		NIST
I	1495.00		NIST
I	1494.00		NIST
I	1493.00		NIST
I	1489.00		NIST
I	1496.00		NIST
I	1496.00		NIST
I	1496.00		NIST
I	1496.00		NIST
I	1496.00		NIST
I	1480.00		NIST
I	1495.00		NIST
I	1518.00		NIST
I	1476.00		NIST
I	1481.00		NIST
I	1482.00		NIST
I	1470.00		NIST
I	1492.00		NIST
I	1465.00		NIST
I	1502.00		NIST
I	1483.00		NIST
I	1501.00		NIST
I	1515.00		NIST
I	1499.00		NIST
I	1484.00		NIST
I	1475.00		NIST
I	Outlier 1458.00		NIST
I	Outlier 1453.00		NIST
I	1492.00		NIST
I	1488.00		NIST
I	1490.00		NIST
I	1489.00		NIST
S°_liquid	347.00	J/mol×K	NIST
T_boil	[449.65; 458.20]	K
T_boil	458.20	K	(Liquid + liquid) equilibria of (water + propionic acid + 2-ethyl-1-hexanol): Experimental data and correlation
T_boil	457.77	K	KDB
T_boil	457.70	K	NIST
T_boil	457.45	K	NIST
T_boil	457.15 ± 3.00	K	NIST
T_boil	457.49 ± 0.50	K	NIST
T_boil	456.15 ± 3.00	K	NIST
T_boil	456.15 ± 3.00	K	NIST
T_boil	Outlier 449.65 ± 3.00	K	NIST
T_boil	457.95	K	NIST
T_boil	454.90 ± 3.00	K	NIST
T_boil	456.65 ± 3.00	K	NIST
T_boil	456.15 ± 3.00	K	NIST
T_boil	454.15 ± 3.00	K	NIST
T_boil	453.65 ± 3.00	K	NIST
T_boil	454.65 ± 3.00	K	NIST
T_boil	455.15 ± 3.00	K	NIST
T_boil	454.15 ± 3.00	K	NIST
T_boil	454.80 ± 3.00	K	NIST
T_boil	457.00 ± 3.00	K	NIST
T_boil	457.80 ± 1.00	K	NIST
T_boil	453.65 ± 3.00	K	NIST
T_boil	457.75 ± 2.00	K	NIST
T_boil	453.15 ± 3.00	K	NIST
T_boil	455.65 ± 5.00	K	NIST
T_c	[640.20; 641.00]	K
T_c	640.60	K	KDB
T_c	641.00 ± 1.00	K	NIST
T_c	641.00 ± 2.00	K	NIST
T_c	640.20 ± 0.30	K	NIST
T_fus	203.00	K	KDB
V_c	0.456	m³/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
C_p,gas	[290.23; 354.79]	J/mol×K	[474.18; 637.10]

C_p,gas	290.23	J/mol×K	474.18	Joback Calculated Property
C_p,gas	302.08	J/mol×K	501.33	Joback Calculated Property
C_p,gas	313.47	J/mol×K	528.49	Joback Calculated Property
C_p,gas	324.43	J/mol×K	555.64	Joback Calculated Property
C_p,gas	334.96	J/mol×K	582.79	Joback Calculated Property
C_p,gas	345.08	J/mol×K	609.94	Joback Calculated Property
C_p,gas	354.79	J/mol×K	637.10	Joback Calculated Property
C_p,liquid	317.50	J/mol×K	298.15	NIST
η	[0.0001689; 0.1178389]	Pa×s	[225.74; 474.18]

η	0.1178389	Pa×s	225.74	Joback Calculated Property
η	0.0169844	Pa×s	267.15	Joback Calculated Property
η	0.0041171	Pa×s	308.55	Joback Calculated Property
η	0.0013956	Pa×s	349.96	Joback Calculated Property
η	0.0005948	Pa×s	391.37	Joback Calculated Property
η	0.0002984	Pa×s	432.77	Joback Calculated Property
η	0.0001689	Pa×s	474.18	Joback Calculated Property
Δ_vapH	[52.70; 60.20]	kJ/mol	[385.50; 402.00]
Δ_vapH	52.70	kJ/mol	385.50	NIST
Δ_vapH	60.20	kJ/mol	402.00	NIST
P_vap	[0.02; 103.26]	kPa	[293.80; 458.24]

P_vap	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
P_vap	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
P_vap	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
P_vap	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
P_vap	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
P_vap	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
P_vap	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
P_vap	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
P_vap	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
P_vap	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
P_vap	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
P_vap	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
P_vap	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
P_vap	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
P_vap	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
P_vap	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
P_vap	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
P_vap	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
P_vap	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
P_vap	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
P_vap	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
P_vap	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
P_vap	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
P_vap	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
P_vap	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
P_vap	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
P_vap	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
P_vap	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
P_vap	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
P_vap	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
P_vap	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
ρ_l	[821.68; 833.00]	kg/m³	[293.00; 308.15]
ρ_l	833.00	kg/m³	293.00	KDB
ρ_l	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
ρ_l	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
ρ_l	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
c_sound,fluid	[1318.07; 1318.44]	m/s	[298.15; 298.15]
c_sound,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
c_sound,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
P_vap	[1.33; 202.63]	kPa	[349.00; 482.60]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
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

P_vap	1.33	kPa	349.00	Calculated Property
P_vap	3.02	kPa	363.84	Calculated Property
P_vap	6.25	kPa	378.69	Calculated Property
P_vap	11.99	kPa	393.53	Calculated Property
P_vap	21.57	kPa	408.38	Calculated Property
P_vap	36.73	kPa	423.22	Calculated Property
P_vap	59.63	kPa	438.07	Calculated Property
P_vap	92.85	kPa	452.91	Calculated Property
P_vap	139.39	kPa	467.76	Calculated Property
P_vap	202.63	kPa	482.60	Calculated Property
P_vap	[7.91e-10; 2836.74]	kPa	[203.15; 640.25]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + Cln(T) + DT^2
Coefficient A			3.04517e+02
Coefficient B			-2.04556e+04
Coefficient C			-4.24888e+01
Coefficient D			2.42482e-05
Temperature range, min.			203.15
Temperature range, max.			640.25

P_vap	7.91e-10	kPa	203.15	Calculated Property
P_vap	4.10e-05	kPa	251.72	Calculated Property
P_vap	0.02	kPa	300.28	Calculated Property
P_vap	1.08	kPa	348.85	Calculated Property
P_vap	13.20	kPa	397.42	Calculated Property
P_vap	72.22	kPa	445.98	Calculated Property
P_vap	244.60	kPa	494.55	Calculated Property
P_vap	626.49	kPa	543.12	Calculated Property
P_vap	1378.79	kPa	591.68	Calculated Property
P_vap	2836.74	kPa	640.25	Calculated Property

Similar Compounds

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

Mixtures

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

Sources

KDB Vapor Pressure Data
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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Chemical Properties of 1-Hexanol, 2-ethyl- (CAS 104-76-7)