Chemical Properties of Cyclohexanol (CAS 108-93-0)

InChI

InChI=1S/C6H12O/c7-6-4-2-1-3-5-6/h6-7H,1-5H2

InChI Key

HPXRVTGHNJAIIH-UHFFFAOYSA-N

Formula

C6H12O

SMILES

OC1CCCCC1

Molecular Weight¹

100.16

CAS

108-93-0

Other Names

• 1-Cyclohexanol
• Adronal
• Adronol
• Anol
• Cicloesanolo
• Cyclohexane, hydroxy-
• Cykloheksanol
• Hexahydrophenol
• Hexalin
• Hydralin
• Hydrophenol
• Hydroxycyclohexane
• NSC 403656
• Naxol
• Phenol, hexahydro-
• cyclohexyl alcohol

• ω : Acentric Factor.
• T_ig : Autoignition Temperature (K).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• ε_r : Dielectric Constant (Relative permittivity).
• 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).
• R_g : Radius of Gyration.
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_subH : Enthalpy of sublimation at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• NFPA Safety : NFPA Safety Rating.
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_c : Critical density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I_p : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_gas : Molar entropy at standard conditions (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_boil(P) : Boiling point at given pressure (K).
• T_c : Critical Temperature (K).
• λ_gas : Gas thermal conductivity (W/m×K).
• λ_liquid : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• U_Qi : UNIQUAC Qi Parameter.
• U_Ri : UNIQUAC Ri Parameter.
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.3690; 0.5280]
ω	0.3695		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.3690		ChemSep v8.3 pure component data Compiled value
ω	0.5280		KDB
Tig	[573.15; 573.15]	K
Tig	573.15	K	KDB
Tig	573.15	K	NCMS SOLV-DB
ΔcH°liquid	[-3753.00; -3720.83]	kJ/mol
ΔcH°liquid	-3726.00 ± 2.00	kJ/mol	NIST
ΔcH°liquid	-3728.70 ± 2.20	kJ/mol	NIST
ΔcH°liquid	-3727.00 ± 1.80	kJ/mol	NIST
ΔcH°liquid	-3722.50	kJ/mol	NIST
ΔcH°liquid	-3720.83	kJ/mol	NIST
ΔcH°liquid	Outlier -3753.00	kJ/mol	NIST
μ	[1.70; 1.86]	debye
μ	1.86	debye	ChemSep v8.3 pure component data Compiled value
μ	1.70	debye	KDB
εr	15.00		NCMS SOLV-DB
Tflash,cc	[341.15; 344.26]	K
Tflash,cc	344.26	K	KDB
Tflash,cc	341.15	K	NCMS SOLV-DB
Tflash,oc	340.93	K	KDB
ΔfG°	[-118.00; -109.50]	kJ/mol
ΔfG°	-109.50	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	-118.00	kJ/mol	KDB
Rg	3.4340		KDB
ΔfH°gas	[-298.00; -286.20]	kJ/mol
ΔfH°gas	-286.20	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-294.80	kJ/mol	KDB
ΔfH°gas	-286.80	kJ/mol	NIST
ΔfH°gas	-290.80	kJ/mol	NIST
ΔfH°gas	-288.80	kJ/mol	NIST
ΔfH°gas	-286.20	kJ/mol	NIST
ΔfH°gas	-288.00	kJ/mol	NIST
ΔfH°gas	-298.00	kJ/mol	NIST
ΔfH°liquid	[-359.20; -347.40]	kJ/mol
ΔfH°liquid	-352.00 ± 0.67	kJ/mol	NIST
ΔfH°liquid	-350.00 ± 2.00	kJ/mol	NIST
ΔfH°liquid	-347.40 ± 2.20	kJ/mol	NIST
ΔfH°liquid	-349.20 ± 0.20	kJ/mol	NIST
ΔfH°liquid	-359.20	kJ/mol	NIST
ΔfusH°	7.22	kJ/mol	Joback Calculated Property
ΔvapH°	[42.43; 63.50]	kJ/mol
ΔvapH°	62.01	kJ/mol	NCMS SOLV-DB
ΔvapH°	62.02	kJ/mol	NIST
ΔvapH°	62.00 ± 0.30	kJ/mol	NIST
ΔvapH°	61.80 ± 0.60	kJ/mol	NIST
ΔvapH°	63.50 ± 0.70	kJ/mol	NIST
ΔvapH°	61.30	kJ/mol	NIST
ΔvapH°	62.00 ± 0.90	kJ/mol	NIST
ΔvapH°	62.00 ± 0.20	kJ/mol	NIST
ΔvapH°	62.00 ± 0.30	kJ/mol	NIST
ΔvapH°	62.01	kJ/mol	NIST
ΔvapH°	61.20	kJ/mol	NIST
ΔvapH°	Outlier 42.43	kJ/mol	NIST
IE	[9.75; 10.00]	eV
IE	9.75	eV	NIST
IE	10.00 ± 0.20	eV	NIST
IE	10.00	eV	NIST
log10WS	[-0.44; -0.44]
log10WS	-0.44		Aq. Solubility Prediction
log10WS	-0.44		Estimated Solubility
logPoct/wat	1.230		NCMS SOLV-DB
McVol	90.410	ml/mol	McGowan Calculated Property
NFPA Fire	[%!d(float64=2); %!d(float64=2)]
NFPA Fire	2		KDB
NFPA Fire	2		NCMS SOLV-DB
NFPA Health	[%!d(float64=1); %!d(float64=1)]
NFPA Health	1		KDB
NFPA Health	1		NCMS SOLV-DB
NFPA Safety	0		NCMS SOLV-DB
Pc	[3749.02; 4401.00]	kPa
Pc	4260.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Pc	4260.00	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	4260.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	4260.00	kPa	KDB
Pc	4080.00 ± 150.00	kPa	NIST
Pc	4401.00 ± 25.00	kPa	NIST
Pc	4260.00 ± 50.00	kPa	NIST
Pc	4260.00 ± 50.00	kPa	NIST
Pc	Outlier 3749.02 ± 151.99	kPa	NIST
Ptriple	0.08	kPa	ChemSep v8.3 pure component data Compiled value
ρc	300.48 ± 10.02	kg/m3	NIST
Inp	[849.00; 928.00]
Inp	851.10		NIST
Inp	Outlier 921.10		NIST
Inp	852.90		NIST
Inp	855.00		NIST
Inp	885.00		NIST
Inp	891.00		NIST
Inp	880.00		NIST
Inp	900.00		NIST
Inp	880.00		NIST
Inp	874.00		NIST
Inp	879.00		NIST
Inp	883.00		NIST
Inp	878.00		NIST
Inp	863.00		NIST
Inp	880.00		NIST
Inp	898.00		NIST
Inp	869.00		NIST
Inp	872.00		NIST
Inp	886.00		NIST
Inp	856.00		NIST
Inp	885.00		NIST
Inp	881.00		NIST
Inp	881.00		NIST
Inp	872.00		NIST
Inp	866.00		NIST
Inp	869.00		NIST
Inp	870.00		NIST
Inp	875.00		NIST
Inp	881.00		NIST
Inp	866.00		NIST
Inp	861.00		NIST
Inp	889.00		NIST
Inp	891.00		NIST
Inp	880.00		NIST
Inp	870.00		NIST
Inp	867.00		NIST
Inp	849.00		NIST
Inp	880.00		NIST
Inp	880.00		NIST
Inp	Outlier 928.00		NIST
Inp	876.00		NIST
Inp	880.00		NIST
Inp	880.00		NIST
Inp	881.00		NIST
Inp	874.00		NIST
Inp	874.00		NIST
Inp	899.00		NIST
Inp	880.00		NIST
Inp	Outlier 913.00		NIST
Inp	876.00		NIST
Inp	874.00		NIST
Ip	[1375.00; 1430.00]
Ip	1377.00		NIST
Ip	1386.00		NIST
Ip	1396.00		NIST
Ip	Outlier 1430.00		NIST
Ip	1403.00		NIST
Ip	1386.00		NIST
Ip	1410.00		NIST
Ip	1375.00		NIST
Ip	1376.00		NIST
Ip	1414.00		NIST
Ip	1407.00		NIST
Ip	1408.00		NIST
Ip	1378.00		NIST
Ip	1410.00		NIST
Ip	1403.00		NIST
Ip	1403.00		NIST
Ip	1403.00		NIST
Ip	1393.00		NIST
Ip	1375.00		NIST
Ip	1392.00		NIST
Ip	1375.00		NIST
Ip	1375.00		NIST
Ip	1375.00		NIST
Ip	1375.00		NIST
Ip	1394.00		NIST
Ip	1375.00		NIST
Ip	1392.00		NIST
Ip	1400.00		NIST
Ip	1375.00		NIST
Ip	1375.00		NIST
Ip	1378.00		NIST
Ip	1393.00		NIST
Ip	1375.00		NIST
Ip	1400.00		NIST
S°gas	353.83	J/mol×K	NIST
S°liquid	[199.60; 203.87]	J/mol×K
S°liquid	203.87	J/mol×K	NIST
S°liquid	199.60	J/mol×K	NIST
Tboil	[394.75; 435.60]	K
Tboil	433.73	K	A New Test System for Distillation Efficiency Experiments at Elevated Liquid Viscosities: Vapor-Liquid Equilibrium and Liquid Viscosity Data for Cyclopentanol + Cyclohexanol
Tboil	433.89	K	Isobaric Vapor-Liquid Equilibria of the Ternary System Methylbutyl Ketone + Nonane + Cyclohexanol
Tboil	434.00	K	ChemSep v8.3 pure component data Compiled value
Tboil	433.99	K	KDB
Tboil	434.25	K	NCMS SOLV-DB
Tboil	Outlier 394.75 ± 0.15	K	NIST
Tboil	434.30	K	NIST
Tboil	434.65 ± 1.00	K	NIST
Tboil	434.40 ± 0.50	K	NIST
Tboil	434.15 ± 1.50	K	NIST
Tboil	430.80 ± 2.00	K	NIST
Tboil	431.00 ± 4.00	K	NIST
Tboil	432.15 ± 1.50	K	NIST
Tboil	433.80 ± 0.30	K	NIST
Tboil	433.80 ± 0.30	K	NIST
Tboil	434.25 ± 0.30	K	NIST
Tboil	433.15 ± 5.00	K	NIST
Tboil	433.80 ± 0.30	K	NIST
Tboil	435.60 ± 0.50	K	NIST
Tboil	433.90 ± 0.50	K	NIST
Tboil	433.80 ± 0.50	K	NIST
Tboil	433.90 ± 0.50	K	NIST
Tboil	433.95 ± 0.50	K	NIST
Tboil	431.00 ± 8.00	K	NIST
Tboil	434.10 ± 2.00	K	NIST
Tboil	432.00 ± 6.00	K	NIST
Tc	[625.15; 650.10]	K
Tc	650.10	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Tc	650.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	650.10	K	ChemSep v8.3 pure component data Compiled value
Tc	650.10	K	KDB
Tc	648.00 ± 2.00	K	NIST
Tc	647.10 ± 0.30	K	NIST
Tc	650.00 ± 2.00	K	NIST
Tc	650.00 ± 2.00	K	NIST
Tc	Outlier 625.15 ± 1.50	K	NIST
Tc	650.00 ± 2.00	K	NIST
Tfus	[290.00; 298.80]	K
Tfus	297.20	K	Vapour liquid equilibria, azeotropic data, excess enthalpies, activity coefficients at infinite dilution and solid liquid equilibria for binary alcohol ketone systems
Tfus	298.80	K	Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Tfus	297.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	296.60	K	ChemSep v8.3 pure component data Compiled value
Tfus	298.61	K	KDB
Tfus	296.62	K	Aq. Solubility Prediction
Tfus	298.30	K	NCMS SOLV-DB
Tfus	297.06 ± 0.50	K	NIST
Tfus	296.20 ± 0.30	K	NIST
Tfus	298.60 ± 0.20	K	NIST
Tfus	298.30 ± 0.20	K	NIST
Tfus	298.00 ± 1.50	K	NIST
Tfus	297.05 ± 0.50	K	NIST
Tfus	297.02 ± 0.20	K	NIST
Tfus	296.00 ± 3.00	K	NIST
Tfus	Outlier 290.00 ± 4.00	K	NIST
Ttriple	[296.60; 299.09]	K
Ttriple	296.60	K	ChemSep v8.3 pure component data Compiled value
Ttriple	299.09 ± 0.02	K	NIST
Ttriple	297.00 ± 0.20	K	NIST
Ttriple	299.09 ± 0.02	K	NIST
Ttriple	297.00 ± 0.20	K	NIST
UQi	3.51		ChemSep v8.3 pure component data Compiled value
URi	4.27		ChemSep v8.3 pure component data Compiled value
Vc	[0.322; 0.327]	m3/kmol
Vc	0.327	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.322	m3/kmol	ChemSep v8.3 pure component data Compiled value
Zc	0.2540000		ChemSep v8.3 pure component data Compiled value
Zra	[0.24; 0.26]
Zra	0.26		ChemSep v8.3 pure component data Compiled value
Zra	0.24		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[174.90; 274.70]	J/mol×K	[290.00; 357.94]
Cp,liquid	174.90	J/mol×K	290.00	NIST
Cp,liquid	212.00	J/mol×K	297.95	NIST
Cp,liquid	220.10	J/mol×K	298.00	NIST
Cp,liquid	214.06	J/mol×K	298.15	NIST
Cp,liquid	209.99	J/mol×K	298.15	NIST
Cp,liquid	209.03	J/mol×K	298.15	NIST
Cp,liquid	213.59	J/mol×K	300.00	NIST
Cp,liquid	218.30	J/mol×K	305.05	Heat capacities of selected cycloalcohols
Cp,liquid	202.50	J/mol×K	305.10	NIST
Cp,liquid	218.60	J/mol×K	305.18	Heat capacities of selected cycloalcohols
Cp,liquid	224.00	J/mol×K	310.00	Heat capacities of selected cycloalcohols
Cp,liquid	223.80	J/mol×K	310.00	Heat capacities of selected cycloalcohols
Cp,liquid	229.70	J/mol×K	315.00	Heat capacities of selected cycloalcohols
Cp,liquid	229.60	J/mol×K	315.00	Heat capacities of selected cycloalcohols
Cp,liquid	235.30	J/mol×K	320.00	Heat capacities of selected cycloalcohols
Cp,liquid	235.50	J/mol×K	320.00	Heat capacities of selected cycloalcohols
Cp,liquid	241.30	J/mol×K	325.00	Heat capacities of selected cycloalcohols
Cp,liquid	241.10	J/mol×K	325.00	Heat capacities of selected cycloalcohols
Cp,liquid	246.70	J/mol×K	330.00	Heat capacities of selected cycloalcohols
Cp,liquid	246.80	J/mol×K	330.00	Heat capacities of selected cycloalcohols
Cp,liquid	252.00	J/mol×K	335.00	Heat capacities of selected cycloalcohols
Cp,liquid	252.20	J/mol×K	335.00	Heat capacities of selected cycloalcohols
Cp,liquid	257.60	J/mol×K	340.00	Heat capacities of selected cycloalcohols
Cp,liquid	257.40	J/mol×K	340.00	Heat capacities of selected cycloalcohols
Cp,liquid	263.00	J/mol×K	345.00	Heat capacities of selected cycloalcohols
Cp,liquid	262.80	J/mol×K	345.00	Heat capacities of selected cycloalcohols
Cp,liquid	268.00	J/mol×K	350.00	Heat capacities of selected cycloalcohols
Cp,liquid	268.00	J/mol×K	350.00	Heat capacities of selected cycloalcohols
Cp,liquid	272.30	J/mol×K	355.00	Heat capacities of selected cycloalcohols
Cp,liquid	272.50	J/mol×K	355.00	Heat capacities of selected cycloalcohols
Cp,liquid	274.70	J/mol×K	357.82	Heat capacities of selected cycloalcohols
Cp,liquid	274.70	J/mol×K	357.94	Heat capacities of selected cycloalcohols
η	0.0410700	Pa×s	298.15	NCMS SOLV-DB
εr	15.71		298.15	Comparative Dielectric Study and Molecular Interactions of Binary Mixtures of (Cyclohexanone + 1-Alkanols) and (Cyclopentanone or Cyclohexanone + Cyclohexanol or Cyclohexane) at T = 298.15 K
ΔfusH	[1.70; 8.21]	kJ/mol	[263.50; 298.20]
ΔfusH	8.21	kJ/mol	263.50	NIST
ΔfusH	1.70	kJ/mol	297.00	NIST
ΔfusH	1.70	kJ/mol	297.00	NIST
ΔfusH	1.70	kJ/mol	297.00	NIST
ΔfusH	1.73	kJ/mol	298.20	NIST
ΔsubH	60.70	kJ/mol	285.00	NIST
ΔvapH	[45.44; 62.70]	kJ/mol	[308.00; 433.70]
ΔvapH	61.20 ± 0.60	kJ/mol	308.00	NIST
ΔvapH	60.40	kJ/mol	309.00	NIST
ΔvapH	58.40	kJ/mol	338.00	NIST
ΔvapH	54.80	kJ/mol	364.50	NIST
ΔvapH	62.70	kJ/mol	367.00	NIST
ΔvapH	59.90	kJ/mol	376.00	NIST
ΔvapH	60.10	kJ/mol	377.50	NIST
ΔvapH	52.60	kJ/mol	400.00	NIST
ΔvapH	55.00	kJ/mol	403.00	NIST
ΔvapH	49.80	kJ/mol	410.00	NIST
ΔvapH	49.30	kJ/mol	418.00	NIST
ΔvapH	45.44	kJ/mol	431.70	NIST
ΔvapH	45.48	kJ/mol	433.70	KDB
Pvap	[0.11; 100.05]	kPa	[298.15; 433.38]
Pvap	0.11	kPa	298.15	NCMS SOLV-DB
Pvap	0.50	kPa	322.25	VLE and LLE Data for the System Cyclohexane + Cyclohexene + Water + Cyclohexanol
Pvap	1.00	kPa	330.95	VLE and LLE Data for the System Cyclohexane + Cyclohexene + Water + Cyclohexanol
Pvap	2.00	kPa	341.70	VLE and LLE Data for the System Cyclohexane + Cyclohexene + Water + Cyclohexanol
Pvap	3.95	kPa	353.80	VLE and LLE Data for the System Cyclohexane + Cyclohexene + Water + Cyclohexanol
Pvap	7.90	kPa	367.25	VLE and LLE Data for the System Cyclohexane + Cyclohexene + Water + Cyclohexanol
Pvap	15.85	kPa	382.40	VLE and LLE Data for the System Cyclohexane + Cyclohexene + Water + Cyclohexanol
Pvap	31.75	kPa	399.50	VLE and LLE Data for the System Cyclohexane + Cyclohexene + Water + Cyclohexanol
Pvap	63.75	kPa	419.05	VLE and LLE Data for the System Cyclohexane + Cyclohexene + Water + Cyclohexanol
Pvap	100.05	kPa	433.30	VLE and LLE Data for the System Cyclohexane + Cyclohexene + Water + Cyclohexanol
Pvap	99.00	kPa	433.38	Vapor-Liquid Equilibria of Cyclohexanone + 2-Cyclohexen-1-one and Cyclohexanol + 2-Cyclohexen-1-one, Validated in a Packed Column Distillation.
n0	[1.46320; 1.46500]		[293.15; 303.15]
n0	1.46390		293.15	Phase equilibria of water + 1-propanol + solvent (n-amyl acetate, cyclohexanol, and cyclohexyl acetate) at T = 298.2K
n0	1.46480		293.20	Phase Equilibria for the Ternary Liquid Systems of (Water + Tetrahydrofurfuryl Alcohol + Cyclic Solvent) at 298.2 K
n0	1.46500		298.15	NCMS SOLV-DB
n0	1.46320		303.15	Experimental study on the calorimetric data of cyclohexanol with alkanols (C1-C4) and correlation with Wilson, NRTL and UNIQUAC models at 300 K
ρl	[941.40; 961.50]	kg/m3	[293.10; 303.20]
ρl	941.40	kg/m3	293.10	Vapor-Liquid Equilibrium for Binary Systems of Cyclohexane + Cyclohexanone and + Cyclohexanol at Temperatures from (414.0 to 433.7) K
ρl	961.50	kg/m3	298.15	Determination and Correlation of Liquid-Liquid Equilibria Data for Water + Cyclohexanol + (Mesityl Oxide, Toluene, and p-Xylene) Ternary Systems at Different Temperatures
ρl	942.00	kg/m3	303.00	KDB
ρl	941.42	kg/m3	303.20	Optimization and modeling of extraction equilibria of the type 2 ternary systems containing (water + isovaleric acid + solvent)
ΔfusS	[5.72; 31.14]	J/mol×K	[263.50; 297.00]
ΔfusS	31.14	J/mol×K	263.50	NIST
ΔfusS	5.72	J/mol×K	297.00	NIST
csound,fluid	[1370.80; 1443.20]	m/s	[303.15; 318.15]
csound,fluid	1443.20	m/s	303.15	Densities, Viscosities, Sound Speed, and IR Studies of N-methyl-2- pyrrolidone with Cyclohexylamine, Cyclohexanol, and Cyclohexene at different Temperatures.
csound,fluid	1419.60	m/s	308.15	Densities, Viscosities, Sound Speed, and IR Studies of N-methyl-2- pyrrolidone with Cyclohexylamine, Cyclohexanol, and Cyclohexene at different Temperatures.
csound,fluid	1395.20	m/s	313.15	Densities, Viscosities, Sound Speed, and IR Studies of N-methyl-2- pyrrolidone with Cyclohexylamine, Cyclohexanol, and Cyclohexene at different Temperatures.
csound,fluid	1370.80	m/s	318.15	Densities, Viscosities, Sound Speed, and IR Studies of N-methyl-2- pyrrolidone with Cyclohexylamine, Cyclohexanol, and Cyclohexene at different Temperatures.
γ	[0.03; 0.03]	N/m	[293.15; 323.15]
γ	0.03	N/m	293.15	Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
γ	0.03	N/m	298.15	Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
γ	0.03	N/m	298.15	NCMS SOLV-DB
γ	0.03	N/m	303.15	Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
γ	0.03	N/m	308.15	Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
γ	0.03	N/m	313.15	Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
γ	0.03	N/m	313.20	KDB
γ	0.03	N/m	318.15	Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
γ	0.03	N/m	323.15	Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboil(P)	[341.68; 417.16]	K	[2.00; 60.00]
Tboil(P)	341.68	K	2.00	A New Test System for Distillation Efficiency Experiments at Elevated Liquid Viscosities: Vapor-Liquid Equilibrium and Liquid Viscosity Data for Cyclopentanol + Cyclohexanol
Tboil(P)	372.00	K	10.00	A New Test System for Distillation Efficiency Experiments at Elevated Liquid Viscosities: Vapor-Liquid Equilibrium and Liquid Viscosity Data for Cyclopentanol + Cyclohexanol
Tboil(P)	387.67	K	20.00	A New Test System for Distillation Efficiency Experiments at Elevated Liquid Viscosities: Vapor-Liquid Equilibrium and Liquid Viscosity Data for Cyclopentanol + Cyclohexanol
Tboil(P)	417.16	K	60.00	A New Test System for Distillation Efficiency Experiments at Elevated Liquid Viscosities: Vapor-Liquid Equilibrium and Liquid Viscosity Data for Cyclopentanol + Cyclohexanol

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[94.93; 382.95]	J/mol×K	[200.00; 1500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A			8.24770e+01
Coefficient B			-8.07950e+02
Coefficient C			6.61824e+00
Coefficient D			-2.87020e-04
Coefficient E			2.50160e-08
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	94.93	J/mol×K	200.00	Calculated Property
Cp,gas	147.63	J/mol×K	344.44	Calculated Property
Cp,gas	207.85	J/mol×K	488.89	Calculated Property
Cp,gas	258.53	J/mol×K	633.33	Calculated Property
Cp,gas	297.63	J/mol×K	777.78	Calculated Property
Cp,gas	326.86	J/mol×K	922.22	Calculated Property
Cp,gas	348.37	J/mol×K	1066.67	Calculated Property
Cp,gas	364.00	J/mol×K	1211.11	Calculated Property
Cp,gas	375.17	J/mol×K	1355.56	Calculated Property
Cp,gas	382.95	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[208.33; 325.78]	J/mol×K	[296.60; 434.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K
Coefficient A			-6.94850e+01
Coefficient B			7.74700e+02
Coefficient C			-2.49106e+00
Coefficient D			2.53840e-02
Coefficient E			-2.29940e-05
Temperature range, min.			296.60
Temperature range, max.			434.00
Cp,liquid	208.33	J/mol×K	296.60	Calculated Property
Cp,liquid	221.43	J/mol×K	311.87	Calculated Property
Cp,liquid	235.52	J/mol×K	327.13	Calculated Property
Cp,liquid	250.16	J/mol×K	342.40	Calculated Property
Cp,liquid	264.94	J/mol×K	357.67	Calculated Property
Cp,liquid	279.42	J/mol×K	372.93	Calculated Property
Cp,liquid	293.17	J/mol×K	388.20	Calculated Property
Cp,liquid	305.75	J/mol×K	403.47	Calculated Property
Cp,liquid	316.76	J/mol×K	418.73	Calculated Property
Cp,liquid	325.78	J/mol×K	434.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0630990; 0.0001989]	Pa×s	[296.60; 520.08]	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			-4.37510e+02
Coefficient B			2.25290e+04
Coefficient C			6.37870e+01
Coefficient D			-4.90010e-05
Coefficient E			2.00000e+00
Temperature range, min.			296.60
Temperature range, max.			520.08
η	0.0630990	Pa×s	296.60	Calculated Property
η	0.0142003	Pa×s	321.43	Calculated Property
η	0.0047644	Pa×s	346.26	Calculated Property
η	0.0021222	Pa×s	371.09	Calculated Property
η	0.0011539	Pa×s	395.92	Calculated Property
η	0.0007199	Pa×s	420.76	Calculated Property
η	0.0004921	Pa×s	445.59	Calculated Property
η	0.0003558	Pa×s	470.42	Calculated Property
η	0.0002649	Pa×s	495.25	Calculated Property
η	0.0001989	Pa×s	520.08	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[61.68; 15.50]	kJ/mol	[296.60; 631.49]	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			7.12884e+01
Coefficient B			3.92061e-01
Coefficient C			-2.16834e+00
Coefficient D			5.55204e+00
Coefficient E			-3.37693e+00
Critical temperature, Tc (K)			6.50100e+02
Temperature range, min.			296.60
Temperature range, max.			631.49
ΔvapH	61.68	kJ/mol	296.60	Calculated Property
ΔvapH	58.04	kJ/mol	333.81	Calculated Property
ΔvapH	53.69	kJ/mol	371.02	Calculated Property
ΔvapH	48.79	kJ/mol	408.23	Calculated Property
ΔvapH	43.54	kJ/mol	445.44	Calculated Property
ΔvapH	38.17	kJ/mol	482.65	Calculated Property
ΔvapH	32.86	kJ/mol	519.86	Calculated Property
ΔvapH	27.71	kJ/mol	557.07	Calculated Property
ΔvapH	22.50	kJ/mol	594.28	Calculated Property
ΔvapH	15.50	kJ/mol	631.49	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[333.32; 457.63]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.45470e+01
Coefficient B			-3.25877e+03
Coefficient C			-1.04780e+02
Temperature range, min.			333.32
Temperature range, max.			457.63
Pvap	1.33	kPa	333.32	Calculated Property
Pvap	3.01	kPa	347.13	Calculated Property
Pvap	6.21	kPa	360.94	Calculated Property
Pvap	11.90	kPa	374.76	Calculated Property
Pvap	21.41	kPa	388.57	Calculated Property
Pvap	36.48	kPa	402.38	Calculated Property
Pvap	59.29	kPa	416.19	Calculated Property
Pvap	92.47	kPa	430.01	Calculated Property
Pvap	139.09	kPa	443.82	Calculated Property
Pvap	202.63	kPa	457.63	Calculated Property
Pvap	[0.16; 4200.70]	kPa	[296.60; 650.10]	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			-3.85449e+01
Coefficient B			-3.98999e+03
Coefficient C			9.01327e+00
Coefficient D			-1.26698e-05
Coefficient E			2.00000e+00
Temperature range, min.			296.60
Temperature range, max.			650.10
Pvap	0.16	kPa	296.60	Calculated Property
Pvap	1.78	kPa	335.88	Calculated Property
Pvap	11.72	kPa	375.16	Calculated Property
Pvap	53.17	kPa	414.43	Calculated Property
Pvap	179.67	kPa	453.71	Calculated Property
Pvap	477.71	kPa	492.99	Calculated Property
Pvap	1040.01	kPa	532.27	Calculated Property
Pvap	1909.43	kPa	571.54	Calculated Property
Pvap	3023.36	kPa	610.82	Calculated Property
Pvap	4200.70	kPa	650.10	Calculated Property
Pvap	[0.09; 3779.27]	kPa	[296.60; 625.15]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			1.29104e+02
Coefficient B			-1.18780e+04
Coefficient C			-1.61598e+01
Coefficient D			5.55366e-06
Coefficient E			0.00000e+00
Temperature range, min.			296.60
Temperature range, max.			625.15
Pvap	0.09	kPa	296.60	Calculated Property
Pvap	1.22	kPa	333.11	Calculated Property
Pvap	8.86	kPa	369.61	Calculated Property
Pvap	40.68	kPa	406.12	Calculated Property
Pvap	134.18	kPa	442.62	Calculated Property
Pvap	347.23	kPa	479.13	Calculated Property
Pvap	750.11	kPa	515.63	Calculated Property
Pvap	1414.27	kPa	552.14	Calculated Property
Pvap	2404.74	kPa	588.64	Calculated Property
Pvap	3779.27	kPa	625.15	Calculated Property
Pvap	[7.50; 98.70]	kPa	[366.88; 433.90]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.16989e+01
Coefficient B			-1.78994e+03
Coefficient C			-1.82037e+02
Reference			Novak, Matous, et al., 1960
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			366.88
Temperature range, max.			433.90
Pvap	7.50	kPa	366.88	Calculated Property
Pvap	10.92	kPa	374.33	Calculated Property
Pvap	15.45	kPa	381.77	Calculated Property
Pvap	21.32	kPa	389.22	Calculated Property
Pvap	28.77	kPa	396.67	Calculated Property
Pvap	38.05	kPa	404.11	Calculated Property
Pvap	49.42	kPa	411.56	Calculated Property
Pvap	63.14	kPa	419.01	Calculated Property
Pvap	79.48	kPa	426.45	Calculated Property
Pvap	98.70	kPa	433.90	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[951.52; 505.20]	kg/m3	[296.60; 631.49]	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			9.09703e+01
Coefficient B			2.77160e-01
Coefficient C			6.50100e+02
Coefficient D			3.06850e-01
Temperature range, min.			296.60
Temperature range, max.			631.49
ρl	951.52	kg/m3	296.60	Calculated Property
ρl	918.14	kg/m3	333.81	Calculated Property
ρl	883.23	kg/m3	371.02	Calculated Property
ρl	846.46	kg/m3	408.23	Calculated Property
ρl	807.33	kg/m3	445.44	Calculated Property
ρl	765.08	kg/m3	482.65	Calculated Property
ρl	718.50	kg/m3	519.86	Calculated Property
ρl	665.35	kg/m3	557.07	Calculated Property
ρl	600.53	kg/m3	594.28	Calculated Property
ρl	505.20	kg/m3	631.49	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.02]	N/m	[298.55; 434.15]	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			6.17163e-02
Coefficient B			-9.66000e-05
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			298.55
Temperature range, max.			434.15
γ	0.03	N/m	298.55	Calculated Property
γ	0.03	N/m	313.62	Calculated Property
γ	0.03	N/m	328.68	Calculated Property
γ	0.03	N/m	343.75	Calculated Property
γ	0.03	N/m	358.82	Calculated Property
γ	0.03	N/m	373.88	Calculated Property
γ	0.02	N/m	388.95	Calculated Property
γ	0.02	N/m	404.02	Calculated Property
γ	0.02	N/m	419.08	Calculated Property
γ	0.02	N/m	434.15	Calculated Property
γ	[0.03; 0.00]	N/m	[289.35; 631.49]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K
Coefficient A			-2.66870e-02
Coefficient B			-3.17240e+00
Coefficient C			-2.41290e+00
Coefficient D			-8.17960e-04
Coefficient E			-1.62570e-06
Temperature range, min.			289.35
Temperature range, max.			631.49
γ	0.03	N/m	289.35	Calculated Property
γ	0.03	N/m	327.37	Calculated Property
γ	0.03	N/m	365.38	Calculated Property
γ	0.02	N/m	403.40	Calculated Property
γ	0.02	N/m	441.41	Calculated Property
γ	0.01	N/m	479.43	Calculated Property
γ	0.01	N/m	517.44	Calculated Property
γ	0.01	N/m	555.46	Calculated Property
γ	0.00	N/m	593.47	Calculated Property
γ	0.00	N/m	631.49	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.10]	W/m×K	[296.60; 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			3.03490e-03
Coefficient B			6.09700e-01
Coefficient C			6.69350e+02
Coefficient D			4.78820e+05
Temperature range, min.			296.60
Temperature range, max.			1000.00
λgas	0.01	W/m×K	296.60	Calculated Property
λgas	0.02	W/m×K	374.76	Calculated Property
λgas	0.03	W/m×K	452.91	Calculated Property
λgas	0.04	W/m×K	531.07	Calculated Property
λgas	0.04	W/m×K	609.22	Calculated Property
λgas	0.05	W/m×K	687.38	Calculated Property
λgas	0.06	W/m×K	765.53	Calculated Property
λgas	0.07	W/m×K	843.69	Calculated Property
λgas	0.09	W/m×K	921.84	Calculated Property
λgas	0.10	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.14; 0.10]	W/m×K	[293.15; 563.15]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K
Coefficient A			7.51870e-02
Coefficient B			-2.49810e+02
Coefficient C			-1.67840e-01
Coefficient D			-6.82330e-03
Coefficient E			2.68820e-06
Temperature range, min.			293.15
Temperature range, max.			563.15
λliquid	0.14	W/m×K	293.15	Calculated Property
λliquid	0.13	W/m×K	323.15	Calculated Property
λliquid	0.13	W/m×K	353.15	Calculated Property
λliquid	0.12	W/m×K	383.15	Calculated Property
λliquid	0.12	W/m×K	413.15	Calculated Property
λliquid	0.11	W/m×K	443.15	Calculated Property
λliquid	0.11	W/m×K	473.15	Calculated Property
λliquid	0.11	W/m×K	503.15	Calculated Property
λliquid	0.11	W/m×K	533.15	Calculated Property
λliquid	0.10	W/m×K	563.15	Calculated Property

Similar Compounds

Find more compounds similar to Cyclohexanol.

Mixtures

• Cyclohexanol + Cyclohexane + Water
• Cyclohexanol + Propanoic acid, 2-oxo- + Water
• Cyclohexanol + Hexanedioic acid
• Cyclohexanol + Water
• Cyclohexanol + 1-Propanol + Water
• Cyclohexanol + Hexanedioic acid + Cyclohexane
• Cyclohexanol + Hexanedioic acid + Cyclohexanone
• Cyclohexanol + 2-Pyrrolidinone, 1-methyl-
• Cyclohexanol + Heptane + Water
• Cyclohexanol + Toluene + Water
• Cyclohexanol + Cyclohexylamine + Water
• Cyclohexanol + Toluene
• Cyclohexanol + Cyclohexane
• Cyclohexanol + 1,4-Dioxane + Water
• Cyclohexanol + Oxygen
• Cyclohexanol + Carbon dioxide
• Cyclohexanol + Cyclohexanone
• Cyclohexanol + Methyl Alcohol
• Cyclohexanol + 1-Propanol
• Cyclohexanol + 1-Butanol

Find more mixtures with Cyclohexanol.

Sources

• KDB Vapor Pressure Data
• Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
• IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 ChEDL chemicals 1.5.2, from Gude, M.; Teja, A. S. Vapor-Liquid Critical Properties of Elements and Compounds. 4. Aliphatic Alkanols. J. Chem. Eng. Data 1995, 40, 1025-1036.
• Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
• PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
• ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
• Phase equilibria of water + 1-propanol + solvent (n-amyl acetate, cyclohexanol, and cyclohexyl acetate) at T = 298.2K
• Vapour liquid equilibria, azeotropic data, excess enthalpies, activity coefficients at infinite dilution and solid liquid equilibria for binary alcohol ketone systems
• "Vapor-liquid" equilibrium measurements and modeling for the cyclohexane + cyclohexanol binary system
• Liquid-liquid equilibrium for the system water + 1,4-dioxane + cyclohexanol over the temperature range of 313.2 - 343.2 K
• Measurement on the solubility of adipic acid in various solvents at high temperature and its thermodynamics parameters.
• Distribution of cyclohexanol and cyclohexanone between water and cyclohexane
• Solubilities of adipic acid in binary cyclohexanone + cyclohexanol, cyclohexane + cyclohexanol, and cyclohexane + cyclohexanone solvent mixtures
• Measurement and prediction of liquid-liquid equilibria in ternary systems containing water, an organic component, and cyclohexanol
• Partial molar volumes of organic solutes in water. XIX. Cyclic alcohols(aq) at T = (298 to 573) K and at pressures up to 30 MPa
• Gas solubility of carbon dioxide and of oxygen in cyclohexanol by experiment and molecular simulation
• Experimental study on the calorimetric data of cyclohexanol with alkanols (C1-C4) and correlation with Wilson, NRTL and UNIQUAC models at 300 K
• Phase equilibria of ternary systems (water + pyruvic acid + high boiling alcohol). Thermodynamic modeling and optimization of extraction
• Optimization and modeling of extraction equilibria of the type 2 ternary systems containing (water + isovaleric acid + solvent)
• Densities, Viscosities, Sound Speed, and IR Studies of N-methyl-2- pyrrolidone with Cyclohexylamine, Cyclohexanol, and Cyclohexene at different Temperatures.
• Heat capacities of selected cycloalcohols
• Solubilities of Adipic Acid in Cyclohexanol + Cyclohexanone Mixtures and Cyclohexanone + Cyclohexane Mixtures
• Determination and Correlation for the Solubility of Glutaric Acid in Cyclohexane + Cyclohexanol + Cyclohexanone Solvent Mixtures
• Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
• Measurement and Prediction of Vapor Liquid(-Liquid) Equilibria in Ternary Systems Containing Water, an Organic Component, and Cyclohexanol
• Determination and Correlation of Liquid-Liquid Equilibria Data for Water + Cyclohexanol + (Mesityl Oxide, Toluene, and p-Xylene) Ternary Systems at Different Temperatures
• Liquid-Liquid Equilibria for the Ternary Systems Water + Cyclohexanol + Methyl Isobutyl Carbinol and Water + Cyclohexanol + Methyl Isobutyl Ketone at Different Temperatures
• Measurement and Prediction of Vapor-Liquid Equilibria in Ternary Systems Containing an Organic Component, Cyclohexylamine, and Cyclohexanol
• Determination and Correlation for the Solubilities of Succinic Acid in Cyclohexanol + Cyclohexanone + Cyclohexane Solvent Mixtures
• Vapor-Liquid Phase Equilibrium of a Cyclohexene + Water + Cyclohexanol + Isophorone Quaternary System at 500 kPa
• Comparative Dielectric Study and Molecular Interactions of Binary Mixtures of (Cyclohexanone + 1-Alkanols) and (Cyclopentanone or Cyclohexanone + Cyclohexanol or Cyclohexane) at T = 298.15 K
• A New Test System for Distillation Efficiency Experiments at Elevated Liquid Viscosities: Vapor-Liquid Equilibrium and Liquid Viscosity Data for Cyclopentanol + Cyclohexanol
• Measurements and Correlation of Liquid-Liquid Equilibria for the Ternary System Cyclohexanol + Water + Cyclohexyl Formate at 298.2-338.2 K
• Thermochemistry of Branched Ethers: Experimental Study of Chemical Equilibrium in the Reacting System of tert-Amyl Alkyl Ether Synthesis
• Isobaric Vapor-Liquid Equilibria of the Ternary System Methylbutyl Ketone + Nonane + Cyclohexanol
• Thermodynamic Properties of Mixtures Containing Ionic Liquids.4.LLE of Binary Mixtures of [C2MIM][NTf2] with Propan-1-ol, Butan-1-ol, and Pentan-1-ol and [C4MIM][NTf2] with Cyclohexanol and 1,2-Hexanediol Including Studies of the Influence of Small Amounts of Water
• Phase Equilibria for the Ternary Liquid Systems of (Water + Tetrahydrofurfuryl Alcohol + Cyclic Solvent) at 298.2 K
• VLE and LLE Data for the System Cyclohexane + Cyclohexene + Water + Cyclohexanol
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 8. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
• Vapor-Liquid Equilibrium for Binary Systems of Cyclohexane + Cyclohexanone and + Cyclohexanol at Temperatures from (414.0 to 433.7) K
• Measurements and Correlation of Liquid Liquid Equilibria for the Ternary System Water + Cyclohexanol + Cyclohexanone
• Vapor-Liquid Equilibria of Cyclohexanone + 2-Cyclohexen-1-one and Cyclohexanol + 2-Cyclohexen-1-one, Validated in a Packed Column Distillation.
• Phase Behavior of the Reactant and Products of Cyclohexane Oxidation in Compressed CO2
• Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
• Partial Molar Volumes of Cyclic Alcohols at Infinite Dilution in Water at Temperatures T ) (298 to 373) K and Pressure of 0.5 MPa
• Experimental and Theoretical Study of the Phase Equilibria in Ternary Aqueous Mixtures of 1,4-Butanediol with Alcohols at 298.2 K
• (Liquid + Liquid) Equilibria of (Cyclohexane + Dimethyl Sulfoxide + Cyclohexanone) and (Cyclohexane + Dimethyl Sulfoxide + Cyclohexanol) at T = 303.2 K
• Liquid-Liquid Equilibrium for the System Water + Cyclohexene + Cyclohexanol over the Temperature Range of (303.2 to 403.2) K
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• NCMS SOLV-DB
• The Yaws Handbook of Vapor Pressure

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