Chemical Properties of 2-Hexanol (CAS 626-93-7)

InChI

InChI=1S/C6H14O/c1-3-4-5-6(2)7/h6-7H,3-5H2,1-2H3

InChI Key

QNVRIHYSUZMSGM-UHFFFAOYSA-N

Formula

C6H14O

SMILES

CCCCC(C)O

Molecular Weight¹

102.17

CAS

626-93-7

Other Names

• 2-Hexyl alcohol
• 2-hydroxyhexane
• Hexan-2-ol
• Hexanol-(2)
• butylmethylcarbinol
• methyl butyl carbinol
• n-Butylmethylcarbinol
• n-C4H9CH(OH)CH3
• n-Hexan-2-ol
• sec-Hexyl alcohol

• ω : Acentric Factor.
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• 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.
• P_c : Critical 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 : Polar retention indices.
• 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).
• Z_c : Critical Compressibility.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.5800		Relay (1.0) Calculated Property
η	0.0042040	Pa×s	Speeds of sound, isentropic compressibilities, viscosities and excess molar volumes of binary mixtures of methylcyclohexane + 2-alkanols or ethanol at T = 298.15 K
ΔfG°	-139.62	kJ/mol	Joback Calculated Property
ΔfH°gas	[-335.60; -329.90]	kJ/mol
ΔfH°gas	-333.50 ± 2.20	kJ/mol	NIST
ΔfH°gas	-335.60 ± 2.20	kJ/mol	NIST
ΔfH°gas	-329.90 ± 2.10	kJ/mol	NIST
ΔfH°liquid	[-394.10; -388.40]	kJ/mol
ΔfH°liquid	-392.00 ± 0.88	kJ/mol	NIST
ΔfH°liquid	-394.10 ± 0.88	kJ/mol	NIST
ΔfH°liquid	-388.40 ± 0.75	kJ/mol	NIST
ΔfusH°	11.86	kJ/mol	Joback Calculated Property
ΔvapH°	[57.00; 58.47]	kJ/mol
ΔvapH°	58.47	kJ/mol	NIST
ΔvapH°	57.00 ± 0.20	kJ/mol	NIST
ΔvapH°	58.30 ± 0.30	kJ/mol	NIST
IE	[9.80; 10.24]	eV
IE	9.80 ± 0.03	eV	NIST
IE	10.24	eV	NIST
log10WS	[-0.89; -0.89]
log10WS	-0.89		Aq. Solubility Prediction
log10WS	-0.89		Estimated Solubility
logPoct/wat	1.557		Crippen Calculated Property
McVol	101.270	ml/mol	McGowan Calculated Property
NFPA Fire	2		KDB
Pc	[3310.00; 3310.00]	kPa
Pc	3310.00	kPa	KDB
Pc	3310.00 ± 20.00	kPa	NIST
Pc	3310.00 ± 20.00	kPa	NIST
Pc	3310.00 ± 20.00	kPa	NIST
ρc	[265.65; 265.65]	kg/m3
ρc	265.65 ± 2.04	kg/m3	NIST
ρc	265.65 ± 6.13	kg/m3	NIST
Inp	[128.24; 812.60]
Inp	780.30		NIST
Inp	777.70		NIST
Inp	787.60		NIST
Inp	775.90		NIST
Inp	778.50		NIST
Inp	803.10		NIST
Inp	804.40		NIST
Inp	766.00		NIST
Inp	775.00		NIST
Inp	787.00		NIST
Inp	786.00		NIST
Inp	783.00		NIST
Inp	766.00		NIST
Inp	787.00		NIST
Inp	784.00		NIST
Inp	788.00		NIST
Inp	789.00		NIST
Inp	804.00		NIST
Inp	790.00		NIST
Inp	790.00		NIST
Inp	781.00		NIST
Inp	800.00		NIST
Inp	793.00		NIST
Inp	784.00		NIST
Inp	786.00		NIST
Inp	801.00		NIST
Inp	787.00		NIST
Inp	801.00		NIST
Inp	803.00		NIST
Inp	812.60		NIST
Inp	784.00		NIST
Inp	783.00		NIST
Inp	811.00		NIST
Inp	777.00		NIST
Inp	777.00		NIST
Inp	786.00		NIST
Inp	780.00		NIST
Inp	795.00		NIST
Inp	809.00		NIST
Inp	774.00		NIST
Inp	787.00		NIST
Inp	787.00		NIST
Inp	787.00		NIST
Inp	785.00		NIST
Inp	782.00		NIST
Inp	803.00		NIST
Inp	793.00		NIST
Inp	784.00		NIST
Inp	784.00		NIST
Inp	786.00		NIST
Inp	799.00		NIST
Inp	786.00		NIST
Inp	786.00		NIST
Inp	Outlier 128.24		NIST
Inp	803.00		NIST
Inp	777.00		NIST
Inp	809.00		NIST
Inp	780.30		NIST
Inp	803.10		NIST
Inp	786.00		NIST
Inp	787.00		NIST
I	[1179.00; 1254.00]
I	1195.00		NIST
I	1233.00		NIST
I	1226.00		NIST
I	1254.00		NIST
I	1229.00		NIST
I	1219.00		NIST
I	1207.00		NIST
I	1240.00		NIST
I	1226.00		NIST
I	1232.00		NIST
I	1195.00		NIST
I	1232.00		NIST
I	1216.00		NIST
I	1243.00		NIST
I	1222.00		NIST
I	1233.00		NIST
I	1238.00		NIST
I	1211.00		NIST
I	1234.00		NIST
I	1218.00		NIST
I	Outlier 1182.00		NIST
I	1227.00		NIST
I	1217.00		NIST
I	1239.00		NIST
I	1210.00		NIST
I	1241.00		NIST
I	1236.00		NIST
I	Outlier 1182.00		NIST
I	1245.00		NIST
I	1216.00		NIST
I	1192.00		NIST
I	1216.00		NIST
I	1232.00		NIST
I	1220.00		NIST
I	1202.00		NIST
I	1231.00		NIST
I	1238.00		NIST
I	1238.00		NIST
I	Outlier 1179.00		NIST
I	1219.00		NIST
I	1222.00		NIST
I	1191.00		NIST
I	1232.00		NIST
I	1192.00		NIST
I	1192.00		NIST
I	1192.00		NIST
I	1238.00		NIST
I	1232.00		NIST
Tboil	[409.15; 413.35]	K
Tboil	411.00	K	KDB
Tboil	409.20	K	NIST
Tboil	413.00	K	NIST
Tboil	411.15 ± 2.00	K	NIST
Tboil	411.65 ± 1.50	K	NIST
Tboil	413.15 ± 0.50	K	NIST
Tboil	413.05 ± 0.50	K	NIST
Tboil	411.15 ± 3.00	K	NIST
Tboil	412.65 ± 2.00	K	NIST
Tboil	410.15 ± 3.00	K	NIST
Tboil	412.55 ± 1.00	K	NIST
Tboil	411.65 ± 3.00	K	NIST
Tboil	409.65 ± 2.00	K	NIST
Tboil	412.65 ± 1.00	K	NIST
Tboil	409.15 ± 2.00	K	NIST
Tboil	411.65 ± 2.00	K	NIST
Tboil	412.95 ± 0.30	K	NIST
Tboil	411.65 ± 2.00	K	NIST
Tboil	413.35 ± 0.50	K	NIST
Tboil	412.65 ± 1.00	K	NIST
Tboil	410.15 ± 2.00	K	NIST
Tboil	412.65 ± 0.70	K	NIST
Tboil	410.65 ± 2.00	K	NIST
Tboil	409.15 ± 2.00	K	NIST
Tboil	409.15 ± 2.00	K	NIST
Tc	[568.20; 586.20]	K
Tc	585.90	K	KDB
Tc	585.90 ± 0.50	K	NIST
Tc	585.40 ± 0.60	K	NIST
Tc	585.40 ± 0.60	K	NIST
Tc	585.80	K	NIST
Tc	586.01 ± 0.30	K	NIST
Tc	Outlier 568.20	K	NIST
Tc	586.20 ± 0.30	K	NIST
Tfus	213.29	K	Relay (1.0) Calculated Property
Vc	[0.384; 0.384]	m3/kmol
Vc	0.384	m3/kmol	KDB
Vc	0.384	m3/kmol	NIST
Zc	0.2609150		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[207.74; 261.25]	J/mol×K	[428.42; 592.97]
Cp,gas	207.74	J/mol×K	428.42	Joback Calculated Property
Cp,gas	217.54	J/mol×K	455.85	Joback Calculated Property
Cp,gas	226.97	J/mol×K	483.27	Joback Calculated Property
Cp,gas	236.05	J/mol×K	510.70	Joback Calculated Property
Cp,gas	244.78	J/mol×K	538.12	Joback Calculated Property
Cp,gas	253.18	J/mol×K	565.55	Joback Calculated Property
Cp,gas	261.25	J/mol×K	592.97	Joback Calculated Property
Cp,liquid	[256.31; 260.34]	J/mol×K	[298.15; 298.15]
Cp,liquid	256.31	J/mol×K	298.15	NIST
Cp,liquid	260.34	J/mol×K	298.15	NIST
η	[0.0016400; 0.0041010]	Pa×s	[298.15; 323.15]
η	0.0041010	Pa×s	298.15	Densities and viscosities of binary mixtures of ethylmethylketone and 2-alkanols; application of the ERAS model and cubic EOS
η	0.0041010	Pa×s	298.15	Densities and Viscosities of Binary Mixtures of Cyclohexanone and 2-Alkanols
η	0.0034110	Pa×s	303.15	Densities and viscosities of binary mixtures of ethylmethylketone and 2-alkanols; application of the ERAS model and cubic EOS
η	0.0032300	Pa×s	303.15	Density and Viscosity Measurement of n-Butylamine with Hexyl Alcohol Isomer Binary Systems
η	0.0034110	Pa×s	303.15	Densities and Viscosities of Binary Mixtures of Cyclohexanone and 2-Alkanols
η	0.0028190	Pa×s	308.15	Densities and viscosities of binary mixtures of ethylmethylketone and 2-alkanols; application of the ERAS model and cubic EOS
η	0.0028190	Pa×s	308.15	Densities and Viscosities of Binary Mixtures of Cyclohexanone and 2-Alkanols
η	0.0022190	Pa×s	313.15	Densities and viscosities of binary mixtures of ethylmethylketone and 2-alkanols; application of the ERAS model and cubic EOS
η	0.0022900	Pa×s	313.15	Density and Viscosity Measurement of n-Butylamine with Hexyl Alcohol Isomer Binary Systems
η	0.0022190	Pa×s	313.15	Densities and Viscosities of Binary Mixtures of Cyclohexanone and 2-Alkanols
η	0.0016400	Pa×s	323.15	Density and Viscosity Measurement of n-Butylamine with Hexyl Alcohol Isomer Binary Systems
ΔvapH	[41.01; 61.80]	kJ/mol	[273.50; 413.00]
ΔvapH	61.80	kJ/mol	273.50	NIST
ΔvapH	56.80 ± 0.20	kJ/mol	313.00	NIST
ΔvapH	55.00 ± 0.20	kJ/mol	328.00	NIST
ΔvapH	53.00 ± 0.20	kJ/mol	343.00	NIST
ΔvapH	49.70	kJ/mol	355.50	NIST
ΔvapH	50.70 ± 0.20	kJ/mol	358.00	NIST
ΔvapH	53.10	kJ/mol	358.00	NIST
ΔvapH	49.20 ± 0.20	kJ/mol	368.00	NIST
ΔvapH	52.40	kJ/mol	375.00	NIST
ΔvapH	47.80	kJ/mol	381.50	NIST
ΔvapH	48.70	kJ/mol	387.50	NIST
ΔvapH	41.01	kJ/mol	413.00	NIST
Pvap	[0.04; 0.69]	kPa	[274.50; 309.40]
Pvap	0.04	kPa	274.50	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	0.04	kPa	275.50	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	276.30	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	276.50	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	0.06	kPa	278.30	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	279.50	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	0.07	kPa	281.30	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	282.20	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	282.50	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	0.10	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	0.10	kPa	285.40	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	0.10	kPa	285.50	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	0.12	kPa	287.50	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	0.13	kPa	288.40	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	0.16	kPa	290.50	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	0.17	kPa	291.40	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	0.18	kPa	292.10	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.19	kPa	293.20	Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap	0.20	kPa	293.40	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	0.21	kPa	294.40	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	0.25	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	0.26	kPa	296.50	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	0.27	kPa	297.40	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	0.33	kPa	299.50	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	0.34	kPa	300.40	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	0.41	kPa	302.50	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	0.42	kPa	303.40	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	0.52	kPa	305.50	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	0.53	kPa	306.40	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	0.60	kPa	307.60	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	0.69	kPa	309.40	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
n0	[1.40770; 1.41350]		[293.15; 308.15]
n0	1.41350		293.15	Densities, viscosities, excess molar volumes, and refractive indices of acetonitrile and 2-alkanols binary mixtures at different temperatures: Experimental results and application of the Prigogine Flory Patterson theory
n0	1.41160		298.15	Densities, viscosities, excess molar volumes, and refractive indices of acetonitrile and 2-alkanols binary mixtures at different temperatures: Experimental results and application of the Prigogine Flory Patterson theory
n0	1.41160		298.15	Densities, Viscosities, and Refractive Indices of Binary Mixtures of Acetophenone and 2-Alkanols
n0	1.40930		303.15	Densities, viscosities, excess molar volumes, and refractive indices of acetonitrile and 2-alkanols binary mixtures at different temperatures: Experimental results and application of the Prigogine Flory Patterson theory
n0	1.40770		308.15	Densities, viscosities, excess molar volumes, and refractive indices of acetonitrile and 2-alkanols binary mixtures at different temperatures: Experimental results and application of the Prigogine Flory Patterson theory
ρl	[784.60; 818.06]	kg/m3	[288.15; 328.15]
ρl	818.06	kg/m3	288.15	Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
ρl	816.00	kg/m3	293.00	KDB
ρl	814.17	kg/m3	293.15	Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
ρl	810.84	kg/m3	298.15	Study of thermodynamic and transport properties of binary liquid mixtures of n-decane with hexan-2-ol, heptan-2-ol and octan-2-ol at T = 298.15 K. Experimental results and application of the Prigogine-Flory-Patterson theory
ρl	810.14	kg/m3	298.15	Densities and viscosities of the mixtures (formamide + 2-alkanol): Experimental and theoretical approaches
ρl	810.10	kg/m3	298.15	Thermodynamic Properties of Binary Mixtures Containing N,N-Dimethylacetamide + 2-Alkanol: Experimental Data and Modeling
ρl	810.17	kg/m3	298.15	The study of physico-chemical properties of binary systems consisting of N-Methylcyclohexylamine with 2-alkanols at T = (298.15-328.15) K
ρl	810.84	kg/m3	298.15	Densities, viscosities and ultrasonic velocities of binary mixtures of methylbenzene with hexan-2-ol, heptan-2-ol and octan-2-ol at T = 298.15 and 308.15K
ρl	810.23	kg/m3	298.15	Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
ρl	806.13	kg/m3	303.15	Densities and viscosities of the mixtures (formamide + 2-alkanol): Experimental and theoretical approaches
ρl	806.10	kg/m3	303.15	Thermodynamic Properties of Binary Mixtures Containing N,N-Dimethylacetamide + 2-Alkanol: Experimental Data and Modeling
ρl	806.23	kg/m3	303.15	Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
ρl	802.16	kg/m3	308.15	Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
ρl	801.94	kg/m3	308.15	The study of physico-chemical properties of binary systems consisting of N-Methylcyclohexylamine with 2-alkanols at T = (298.15-328.15) K
ρl	802.06	kg/m3	308.15	Densities and viscosities of the mixtures (formamide + 2-alkanol): Experimental and theoretical approaches
ρl	802.10	kg/m3	308.15	Thermodynamic Properties of Binary Mixtures Containing N,N-Dimethylacetamide + 2-Alkanol: Experimental Data and Modeling
ρl	801.75	kg/m3	308.15	Densities, viscosities and ultrasonic velocities of binary mixtures of methylbenzene with hexan-2-ol, heptan-2-ol and octan-2-ol at T = 298.15 and 308.15K
ρl	798.04	kg/m3	313.15	Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
ρl	797.96	kg/m3	313.15	Densities and viscosities of the mixtures (formamide + 2-alkanol): Experimental and theoretical approaches
ρl	798.00	kg/m3	313.15	Thermodynamic Properties of Binary Mixtures Containing N,N-Dimethylacetamide + 2-Alkanol: Experimental Data and Modeling
ρl	793.57	kg/m3	318.15	The study of physico-chemical properties of binary systems consisting of N-Methylcyclohexylamine with 2-alkanols at T = (298.15-328.15) K
ρl	784.60	kg/m3	328.15	The study of physico-chemical properties of binary systems consisting of N-Methylcyclohexylamine with 2-alkanols at T = (298.15-328.15) K

Datasets

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
313.13	1010.00	799.26
313.13	2006.00	800.05
313.13	2999.00	800.83
313.13	4008.00	801.59
313.13	4999.00	802.35
313.13	5986.00	803.12
313.13	7000.00	803.86
313.13	8010.00	804.64
313.13	9026.00	805.38
313.13	10004.00	806.09
313.13	11005.00	806.84
313.13	12001.00	807.56
313.13	13010.00	808.28
313.13	14002.00	808.98
313.13	14998.00	809.67
313.13	16001.00	810.39
313.13	17006.00	811.08
313.13	18000.00	811.7
313.13	19005.00	812.39
313.13	20015.00	813.1
313.13	21029.00	813.74
313.13	22004.00	814.4
323.09	1037.00	791.0
323.09	2000.00	791.79
323.09	3010.00	792.63
323.09	4029.00	793.48
323.09	5004.00	794.27
323.09	6020.00	795.1
323.09	7007.00	795.84
323.09	8009.00	796.68
323.09	9017.00	797.48
323.09	10003.00	798.25
323.09	11001.00	799.0
323.09	12000.00	799.77
323.09	13021.00	800.56
323.09	14001.00	801.3
323.09	15002.00	802.0
323.09	16000.00	802.74
323.09	17004.00	803.48
323.09	18008.00	804.21
323.09	19001.00	804.9
323.09	20011.00	805.62
323.09	21003.00	806.31
323.09	22004.00	807.01
333.04	1055.00	782.56
333.04	2007.00	783.43
333.04	3005.00	784.28
333.04	4007.00	785.21
333.04	5015.00	786.06
333.04	6009.00	786.93
333.04	7006.00	787.77
333.04	7998.00	788.61
333.04	9006.00	789.47
333.04	10004.00	790.32
333.04	11007.00	791.11
333.04	12012.00	791.93
333.04	13003.00	792.72
333.04	14008.00	793.51
333.04	15005.00	794.3
333.04	16001.00	795.06
333.04	17006.00	795.85
333.04	18010.00	796.61
333.04	19002.00	797.35
333.04	20000.00	798.08
333.04	21000.00	798.82
333.04	22004.00	799.56
342.98	1032.00	774.05
342.98	2015.00	775.01
342.98	3012.00	775.95
342.98	4017.00	776.87
342.98	5013.00	777.79
342.98	6012.00	778.72
342.98	7025.00	779.62
342.98	8000.00	780.47
342.98	9000.00	781.35
342.98	9996.00	782.25
342.98	11020.00	783.12
342.98	11999.00	783.92
342.98	12996.00	784.76
342.98	14007.00	785.6
342.98	15003.00	786.41
342.98	16005.00	787.17
342.98	17002.00	787.98
342.98	18010.00	788.76
342.98	19005.00	789.49
342.98	20010.00	790.27
342.98	21006.00	791.0
342.98	22005.00	791.75
352.86	1053.00	765.06
352.86	2014.00	766.05
352.86	3019.00	767.09
352.86	4033.00	768.08
352.86	4996.00	769.01
352.86	6006.00	770.06
352.86	7013.00	771.02
352.86	8004.00	771.95
352.86	9035.00	772.93
352.86	10009.00	773.84
352.86	11007.00	774.75
352.86	12007.00	775.66
352.86	12999.00	776.54
352.86	14012.00	777.47
352.86	15010.00	778.33
352.86	16003.00	779.21
352.86	17002.00	780.07
352.86	18017.00	780.92
352.86	19005.00	781.75
352.86	20014.00	782.58
352.86	21013.00	783.39
352.86	22010.00	784.18
362.73	1075.00	754.97
362.73	2006.00	756.02
362.73	3018.00	757.16
362.73	4034.00	758.26
362.73	5016.00	759.29
362.73	6066.00	760.41
362.73	6998.00	761.37
362.73	8041.00	762.44
362.73	9014.00	763.43
362.73	10001.00	764.37
362.73	11026.00	765.39
362.73	12000.00	766.35
362.73	13010.00	767.31
362.73	13999.00	768.28
362.73	15006.00	769.21
362.73	16006.00	770.12
362.73	17005.00	771.02
362.73	18000.00	771.92
362.73	19003.00	772.82
362.73	20017.00	773.7
362.73	21006.00	774.56
362.73	22010.00	775.42
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[314.79; 434.35]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.50376e+01
Coefficient B			-3.41427e+03
Coefficient C			-8.33130e+01
Temperature range, min.			314.79
Temperature range, max.			434.35
Pvap	1.33	kPa	314.79	Calculated Property
Pvap	2.97	kPa	328.07	Calculated Property
Pvap	6.09	kPa	341.36	Calculated Property
Pvap	11.64	kPa	354.64	Calculated Property
Pvap	20.94	kPa	367.93	Calculated Property
Pvap	35.75	kPa	381.21	Calculated Property
Pvap	58.31	kPa	394.50	Calculated Property
Pvap	91.37	kPa	407.78	Calculated Property
Pvap	138.22	kPa	421.07	Calculated Property
Pvap	202.63	kPa	434.35	Calculated Property
Pvap	[9.61e-05; 3339.22]	kPa	[223.00; 586.20]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			1.05887e+02
Coefficient B			-1.03384e+04
Coefficient C			-1.27495e+01
Coefficient D			3.27083e-06
Temperature range, min.			223.00
Temperature range, max.			586.20
Pvap	9.61e-05	kPa	223.00	Calculated Property
Pvap	0.01	kPa	263.36	Calculated Property
Pvap	0.48	kPa	303.71	Calculated Property
Pvap	5.80	kPa	344.07	Calculated Property
Pvap	36.42	kPa	384.42	Calculated Property
Pvap	146.08	kPa	424.78	Calculated Property
Pvap	426.73	kPa	465.13	Calculated Property
Pvap	990.25	kPa	505.49	Calculated Property
Pvap	1938.28	kPa	545.84	Calculated Property
Pvap	3339.22	kPa	586.20	Calculated Property

Similar Compounds

Find more compounds similar to 2-Hexanol.

Mixtures

• Cyclohexanamine, N-methyl- + 2-Hexanol
• 2-Hexanol + Cyclohexane, methyl-
• Acetonitrile + 2-Hexanol
• Decane + 2-Hexanol
• Toluene + 2-Hexanol
• Nitrogen + 2-Hexanol
• 2-Hexanol + Ethane, 1,2-dichloro-
• 2-Butanone + 2-Hexanol
• 2-Hexanol + Formamide
• 1-Butanamine + 2-Hexanol
• N,N-Dimethylacetamide + 2-Hexanol
• Acetophenone + 2-Hexanol
• Cyclohexanone + 2-Hexanol
• 2-Hexanol + Ethanol, 2,2'-oxybis-

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Vapor liquid equilibria for nitrogen with 2-hexanol, 2-heptanol, or 2-octanol binary systems
• Densities, viscosities and ultrasonic velocities of binary mixtures of methylbenzene with hexan-2-ol, heptan-2-ol and octan-2-ol at T = 298.15 and 308.15K
• A thermodynamic study of the ketoreductase-catalyzed reduction of 2-alkanones in non-aqueous solvents
• Speeds of sound, isentropic compressibilities, viscosities and excess molar volumes of binary mixtures of methylcyclohexane + 2-alkanols or ethanol at T = 298.15 K
• Study of thermodynamic and transport properties of binary liquid mixtures of n-decane with hexan-2-ol, heptan-2-ol and octan-2-ol at T = 298.15 K. Experimental results and application of the Prigogine-Flory-Patterson theory
• Densities and viscosities of the mixtures (formamide + 2-alkanol): Experimental and theoretical approaches
• The study of physico-chemical properties of binary systems consisting of N-Methylcyclohexylamine with 2-alkanols at T = (298.15-328.15) K
• Densities, viscosities, excess molar volumes, and refractive indices of acetonitrile and 2-alkanols binary mixtures at different temperatures: Experimental results and application of the Prigogine Flory Patterson theory
• Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
• Densities and viscosities of binary mixtures of ethylmethylketone and 2-alkanols; application of the ERAS model and cubic EOS
• 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 Viscosity Measurement of n-Butylamine with Hexyl Alcohol Isomer Binary Systems
• Densities and Viscosities of Binary Mixtures of Cyclohexanone and 2-Alkanols
• Densities and Viscosities of Binary Mixtures Containing Diethylene Glycol and 2-Alkanol
• Thermodynamic Properties of Binary Mixtures Containing N,N-Dimethylacetamide + 2-Alkanol: Experimental Data and Modeling
• Refined Flow Microcalorimetric Setup for Measurement of Mixing Enthalpies at High Dilutions: Determination of Infinite Dilution Dissolution Enthalpies of Some Alkanol and Ether Solutes in Water
• Densities, Isothermal Compressibilities, and Isobaric Thermal Expansivities of Hexan-2-ol, Octan-1-ol, and Decan-1-ol from (313 to 363) K and Pressures up to 22 MPa
• Densities, Viscosities, and Refractive Indices of Binary Mixtures of Acetophenone and 2-Alkanols
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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