Chemical Properties of Cyclohexane, ethyl- (CAS 1678-91-7)

InChI

InChI=1S/C8H16/c1-2-8-6-4-3-5-7-8/h8H,2-7H2,1H3

InChI Key

IIEWJVIFRVWJOD-UHFFFAOYSA-N

Formula

C8H16

SMILES

CCC1CCCCC1

Molecular Weight¹

112.21

CAS

1678-91-7

Other Names

• Ethylcyclohexane

• ω : Acentric Factor.
• AP : Aniline Point (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).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_c,grossH : Heat of Combustion, Gross form (kJ/mol).
• Δ_c,netH : Heat of Combustion, Net Form (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_fusH : Enthalpy of fusion 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.
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point 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.
• 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).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• λ_gas : Gas thermal conductivity (W/m×K).
• λ_liquid : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• U_Qi : UNIQUAC Qi Parameter.
• U_Ri : UNIQUAC Ri Parameter.
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.2426; 0.2455]
ω	0.2444		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.2426		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.2455		ChemSep v8.3 pure component data Compiled value
ω	0.2430		KDB
AP	316.950	K	KDB
ΔcH°liquid	-5222.60 ± 1.50	kJ/mol	NIST
μ	[0.00; 0.00]	debye
μ	0.00	debye	ChemSep v8.3 pure component data Compiled value
μ	0.00	debye	KDB
ΔfG°	[39.27; 39.55]	kJ/mol
ΔfG°	39.55	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	39.27	kJ/mol	KDB
Δc,grossH	5222.59	kJ/mol	KDB
Δc,netH	4870.511	kJ/mol	KDB
ΔfH°gas	[-172.60; -171.50]	kJ/mol
ΔfH°gas	-171.50	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-171.90	kJ/mol	KDB
ΔfH°gas	-172.60	kJ/mol	NIST
ΔfH°gas	-171.80 ± 1.50	kJ/mol	NIST
ΔfH°liquid	[-213.00; -212.20]	kJ/mol
ΔfH°liquid	-213.00	kJ/mol	NIST
ΔfH°liquid	-212.20 ± 1.50	kJ/mol	NIST
ΔfusH°	8.31	kJ/mol	Joback Calculated Property
ΔvapH°	[39.20; 40.60]	kJ/mol
ΔvapH°	40.60	kJ/mol	NIST
ΔvapH°	Outlier 39.20 ± 0.40	kJ/mol	NIST
ΔvapH°	40.00 ± 0.40	kJ/mol	NIST
ΔvapH°	40.00 ± 0.40	kJ/mol	NIST
ΔvapH°	40.40	kJ/mol	NIST
ΔvapH°	40.50	kJ/mol	NIST
ΔvapH°	40.50 ± 0.10	kJ/mol	NIST
ΔvapH°	40.47	kJ/mol	NIST
ΔvapH°	40.40	kJ/mol	NIST
IE	[9.54; 9.67]	eV
IE	9.54	eV	NIST
IE	9.67 ± 0.02	eV	NIST
log10WS	[-4.25; -4.25]
log10WS	-4.25		Aq. Solubility Prediction
log10WS	-4.25		Estimated Solubility
logPoct/wat	2.977		Crippen Calculated Property
McVol	112.720	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	1		KDB
Pc	[3000.00; 3250.00]	kPa
Pc	3250.00	kPa	Critical Point Measurements for Five n-Alkylcyclohexanes (C6 to C10) by the Pulse-Heating Method
Pc	3029.62	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	3033.69	kPa	Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc	3040.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	3000.00	kPa	KDB
Ptriple	3.57e-07	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[818.00; 867.90]
Inp	846.00		NIST
Inp	851.00		NIST
Inp	829.00		NIST
Inp	842.20		NIST
Inp	Outlier 859.70		NIST
Inp	Outlier 867.90		NIST
Inp	828.00		NIST
Inp	833.60		NIST
Inp	839.00		NIST
Inp	843.00		NIST
Inp	834.30		NIST
Inp	842.80		NIST
Inp	831.30		NIST
Inp	831.70		NIST
Inp	853.00		NIST
Inp	837.00		NIST
Inp	838.00		NIST
Inp	848.00		NIST
Inp	842.00		NIST
Inp	842.00		NIST
Inp	834.00		NIST
Inp	840.00		NIST
Inp	850.00		NIST
Inp	840.00		NIST
Inp	832.00		NIST
Inp	836.00		NIST
Inp	838.00		NIST
Inp	841.00		NIST
Inp	844.00		NIST
Inp	834.30		NIST
Inp	832.00		NIST
Inp	Outlier 856.00		NIST
Inp	842.00		NIST
Inp	825.00		NIST
Inp	828.00		NIST
Inp	834.00		NIST
Inp	839.00		NIST
Inp	845.00		NIST
Inp	839.00		NIST
Inp	839.00		NIST
Inp	839.00		NIST
Inp	839.00		NIST
Inp	842.00		NIST
Inp	835.92		NIST
Inp	824.00		NIST
Inp	843.00		NIST
Inp	845.00		NIST
Inp	Outlier 854.00		NIST
Inp	840.00		NIST
Inp	832.00		NIST
Inp	841.00		NIST
Inp	832.20		NIST
Inp	829.10		NIST
Inp	828.40		NIST
Inp	826.90		NIST
Inp	829.10		NIST
Inp	830.90		NIST
Inp	838.10		NIST
Inp	830.10		NIST
Inp	Outlier 818.00		NIST
Inp	826.90		NIST
Inp	829.10		NIST
Inp	830.90		NIST
Inp	829.10		NIST
Inp	828.40		NIST
Inp	827.00		NIST
Inp	821.60		NIST
Inp	824.96		NIST
Inp	827.15		NIST
Inp	827.11		NIST
Inp	830.63		NIST
Inp	832.99		NIST
Inp	841.00		NIST
Inp	834.00		NIST
Inp	828.00		NIST
Inp	833.00		NIST
Inp	843.00		NIST
Inp	833.00		NIST
Inp	836.00		NIST
Inp	834.00		NIST
Inp	827.00		NIST
Inp	831.70		NIST
Inp	834.00		NIST
Inp	825.00		NIST
Inp	835.00		NIST
Inp	837.90		NIST
Inp	841.40		NIST
Inp	844.00		NIST
Inp	846.20		NIST
Inp	825.00		NIST
Inp	824.00		NIST
Inp	837.00		NIST
Inp	839.00		NIST
Inp	834.00		NIST
Inp	831.00		NIST
Inp	827.00		NIST
Inp	827.00		NIST
Inp	840.00		NIST
Inp	837.00		NIST
Inp	827.00		NIST
Inp	850.00		NIST
Inp	840.00		NIST
Inp	846.00		NIST
Inp	Outlier 867.90		NIST
Inp	834.30		NIST
Inp	837.00		NIST
Inp	834.00		NIST
Inp	836.00		NIST
Inp	832.00		NIST
Inp	839.00		NIST
Inp	827.00		NIST
Inp	840.00		NIST
Ip	[885.00; 925.20]
Ip	920.00		NIST
Ip	915.00		NIST
Ip	920.00		NIST
Ip	925.20		NIST
Ip	905.50		NIST
Ip	910.10		NIST
Ip	920.00		NIST
Ip	Outlier 885.00		NIST
Ip	920.00		NIST
Ip	910.10		NIST
S°gas	382.67	J/mol×K	NIST
S°liquid	[280.91; 281.60]	J/mol×K
S°liquid	280.91	J/mol×K	NIST
S°liquid	281.60	J/mol×K	NIST
Tboil	[402.00; 410.00]	K
Tboil	404.94	K	ChemSep v8.3 pure component data Compiled value
Tboil	404.90	K	KDB
Tboil	405.00	K	NIST
Tboil	405.00	K	NIST
Tboil	405.00 ± 1.00	K	NIST
Tboil	405.00 ± 2.00	K	NIST
Tboil	406.00 ± 4.00	K	NIST
Tboil	406.00 ± 4.00	K	NIST
Tboil	Outlier 409.00 ± 4.00	K	NIST
Tboil	405.00 ± 1.00	K	NIST
Tboil	405.00 ± 3.00	K	NIST
Tboil	404.00 ± 4.00	K	NIST
Tboil	404.90 ± 0.40	K	NIST
Tboil	404.93 ± 0.20	K	NIST
Tboil	404.93 ± 0.20	K	NIST
Tboil	405.00 ± 0.40	K	NIST
Tboil	403.70 ± 1.00	K	NIST
Tboil	405.00 ± 0.20	K	NIST
Tboil	404.85 ± 0.30	K	NIST
Tboil	404.92 ± 0.30	K	NIST
Tboil	404.35 ± 0.50	K	NIST
Tboil	404.93 ± 0.01	K	NIST
Tboil	405.10 ± 0.50	K	NIST
Tboil	405.00 ± 0.25	K	NIST
Tboil	404.93 ± 0.15	K	NIST
Tboil	404.93 ± 0.10	K	NIST
Tboil	403.15 ± 0.20	K	NIST
Tboil	403.55 ± 0.50	K	NIST
Tboil	404.80 ± 0.80	K	NIST
Tboil	404.75 ± 0.50	K	NIST
Tboil	405.00 ± 2.00	K	NIST
Tboil	404.00 ± 2.00	K	NIST
Tboil	402.65 ± 1.50	K	NIST
Tboil	405.05 ± 0.60	K	NIST
Tboil	403.60 ± 1.50	K	NIST
Tboil	405.00 ± 0.30	K	NIST
Tboil	403.15 ± 3.00	K	NIST
Tboil	402.00 ± 4.00	K	NIST
Tboil	Outlier 410.00 ± 4.00	K	NIST
Tboil	403.00 ± 3.00	K	NIST
Tboil	402.00 ± 3.00	K	NIST
Tc	[605.90; 609.26]	K
Tc	605.90	K	DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
Tc	606.90	K	Gas-Liquid Critical Temperatures of Some Alkenes, Amines, and Cyclic Hydrocarbons
Tc	609.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	609.26	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	609.15	K	ChemSep v8.3 pure component data Compiled value
Tc	609.00	K	KDB
Tc	609.00	K	NIST
Tfus	[158.40; 162.00]	K
Tfus	162.00	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	161.84	K	ChemSep v8.3 pure component data Compiled value
Tfus	161.80	K	KDB
Tfus	162.00	K	Aq. Solubility Prediction
Tfus	Outlier 158.40 ± 1.40	K	NIST
Tfus	161.85 ± 0.05	K	NIST
Tfus	161.80 ± 0.01	K	NIST
Tfus	161.75 ± 0.10	K	NIST
Tfus	159.35 ± 0.30	K	NIST
Tfus	161.75 ± 1.50	K	NIST
Ttriple	[161.40; 161.85]	K
Ttriple	161.85	K	Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple	161.84	K	ChemSep v8.3 pure component data Compiled value
Ttriple	161.84 ± 0.05	K	NIST
Ttriple	161.40 ± 0.20	K	NIST
Ttriple	161.84 ± 0.05	K	NIST
Ttriple	161.40 ± 0.20	K	NIST
UQi	4.32		ChemSep v8.3 pure component data Compiled value
URi	5.39		ChemSep v8.3 pure component data Compiled value
Vc	[0.420; 0.450]	m3/kmol
Vc	0.420	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.430	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.450	m3/kmol	KDB
Zc	[0.2580000; 0.2666120]
Zc	0.2580000		ChemSep v8.3 pure component data Compiled value
Zc	0.2666120		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[152.23; 239.88]	J/mol×K	[298.15; 448.15]
Cp,gas	152.23	J/mol×K	298.15	NIST
Cp,gas	170.36	J/mol×K	323.15	NIST
Cp,gas	197.90	J/mol×K	373.15	NIST
Cp,gas	217.63	J/mol×K	408.15	NIST
Cp,gas	239.88	J/mol×K	448.15	NIST
Cp,liquid	[164.40; 214.20]	J/mol×K	[170.00; 300.00]
Cp,liquid	164.40	J/mol×K	170.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	166.90	J/mol×K	180.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	169.60	J/mol×K	190.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	172.60	J/mol×K	200.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	175.70	J/mol×K	210.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	179.00	J/mol×K	220.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	182.50	J/mol×K	230.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	186.30	J/mol×K	240.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	190.20	J/mol×K	250.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	194.30	J/mol×K	260.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	198.60	J/mol×K	270.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	200.00	J/mol×K	273.15	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	203.20	J/mol×K	280.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	207.90	J/mol×K	290.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	211.90	J/mol×K	298.15	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	211.79	J/mol×K	298.15	NIST
Cp,liquid	214.20	J/mol×K	298.15	NIST
Cp,liquid	212.80	J/mol×K	300.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
ΔfusH	[8.28; 8.50]	kJ/mol	[161.40; 161.84]
ΔfusH	8.33	kJ/mol	161.40	NIST
ΔfusH	8.28	kJ/mol	161.40	NIST
ΔfusH	8.28	kJ/mol	161.40	NIST
ΔfusH	8.28	kJ/mol	161.40	NIST
ΔfusH	8.50	kJ/mol	161.50	NIST
ΔfusH	8.33	kJ/mol	161.84	NIST
ΔfusH	8.33	kJ/mol	161.84	NIST
ΔvapH	[34.04; 39.80]	kJ/mol	[313.00; 405.00]
ΔvapH	39.80 ± 0.10	kJ/mol	313.00	NIST
ΔvapH	38.90 ± 0.10	kJ/mol	328.00	NIST
ΔvapH	37.90 ± 0.10	kJ/mol	343.00	NIST
ΔvapH	37.00 ± 0.10	kJ/mol	358.00	NIST
ΔvapH	38.60	kJ/mol	365.00	NIST
ΔvapH	36.30 ± 0.10	kJ/mol	368.00	NIST
ΔvapH	34.31	kJ/mol	404.90	KDB
ΔvapH	34.04	kJ/mol	405.00	NIST
Pvap	[2.10; 73.20]	kPa	[303.15; 393.15]
Pvap	2.10	kPa	303.15	Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
Pvap	3.70	kPa	313.15	Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
Pvap	6.00	kPa	323.15	Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
Pvap	9.30	kPa	333.15	Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
Pvap	13.90	kPa	343.15	Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
Pvap	20.40	kPa	353.15	Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
Pvap	28.90	kPa	363.15	Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
Pvap	40.30	kPa	373.15	Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
Pvap	54.80	kPa	383.15	Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
Pvap	73.20	kPa	393.15	Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
n0	[1.42750; 1.43073]		[293.15; 298.15]
n0	1.42750		293.15	Density, Viscosity, Refractive Index, and Freezing Point for Binary Mixtures of 1,1'-Bicyclohexyl with Alkylcyclohexane
n0	1.43073		298.15	KDB
ρl	[747.03; 788.02]	kg/m3	[293.00; 343.15]
ρl	788.00	kg/m3	293.00	KDB
ρl	788.02	kg/m3	293.15	Excess Molar Volume along with Viscosity and Refractive Index for Binary Systems of Tricyclo[5.2.1.0(2.6)]decane with Five Cycloalkanes
ρl	787.98	kg/m3	293.15	Densities, Viscosities, Refractive Indices, and Surface Tensions of Binary Mixtures of 2,2,4-Trimethylpentane with Several Alkylated Cyclohexanes from (293.15 to 343.15) K
ρl	787.98	kg/m3	293.15	Density, Viscosity, and Refractive Index of Binary Mixtures of Fatty Acid Ethyl Esters with Ethylcyclohexane
ρl	787.98	kg/m3	293.15	Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Binary Mixtures of Ethylcyclohexane or Methylcyclohexane with n-Dodecane or n-Hexadecane at 0.1 MPa
ρl	783.95	kg/m3	298.15	Density, Viscosity, and Refractive Index of Binary Mixtures of Fatty Acid Ethyl Esters with Ethylcyclohexane
ρl	784.01	kg/m3	298.15	Excess Molar Volume along with Viscosity and Refractive Index for Binary Systems of Tricyclo[5.2.1.0(2.6)]decane with Five Cycloalkanes
ρl	783.97	kg/m3	298.15	Densities, Viscosities, Refractive Indices, and Surface Tensions of Binary Mixtures of 2,2,4-Trimethylpentane with Several Alkylated Cyclohexanes from (293.15 to 343.15) K
ρl	779.98	kg/m3	303.15	Excess Molar Volume along with Viscosity and Refractive Index for Binary Systems of Tricyclo[5.2.1.0(2.6)]decane with Five Cycloalkanes
ρl	779.92	kg/m3	303.15	Density, Viscosity, and Refractive Index of Binary Mixtures of Fatty Acid Ethyl Esters with Ethylcyclohexane
ρl	779.91	kg/m3	303.15	Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Binary Mixtures of Ethylcyclohexane or Methylcyclohexane with n-Dodecane or n-Hexadecane at 0.1 MPa
ρl	779.93	kg/m3	303.15	Densities, Viscosities, Refractive Indices, and Surface Tensions of Binary Mixtures of 2,2,4-Trimethylpentane with Several Alkylated Cyclohexanes from (293.15 to 343.15) K
ρl	775.87	kg/m3	308.15	Density, Viscosity, and Refractive Index of Binary Mixtures of Fatty Acid Ethyl Esters with Ethylcyclohexane
ρl	775.93	kg/m3	308.15	Excess Molar Volume along with Viscosity and Refractive Index for Binary Systems of Tricyclo[5.2.1.0(2.6)]decane with Five Cycloalkanes
ρl	775.88	kg/m3	308.15	Densities, Viscosities, Refractive Indices, and Surface Tensions of Binary Mixtures of 2,2,4-Trimethylpentane with Several Alkylated Cyclohexanes from (293.15 to 343.15) K
ρl	771.79	kg/m3	313.15	Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Binary Mixtures of Ethylcyclohexane or Methylcyclohexane with n-Dodecane or n-Hexadecane at 0.1 MPa
ρl	771.86	kg/m3	313.15	Excess Molar Volume along with Viscosity and Refractive Index for Binary Systems of Tricyclo[5.2.1.0(2.6)]decane with Five Cycloalkanes
ρl	771.80	kg/m3	313.15	Density, Viscosity, and Refractive Index of Binary Mixtures of Fatty Acid Ethyl Esters with Ethylcyclohexane
ρl	771.82	kg/m3	313.15	Densities, Viscosities, Refractive Indices, and Surface Tensions of Binary Mixtures of 2,2,4-Trimethylpentane with Several Alkylated Cyclohexanes from (293.15 to 343.15) K
ρl	767.78	kg/m3	318.15	Excess Molar Volume along with Viscosity and Refractive Index for Binary Systems of Tricyclo[5.2.1.0(2.6)]decane with Five Cycloalkanes
ρl	767.69	kg/m3	318.15	Densities, Viscosities, Refractive Indices, and Surface Tensions of Binary Mixtures of 2,2,4-Trimethylpentane with Several Alkylated Cyclohexanes from (293.15 to 343.15) K
ρl	767.72	kg/m3	318.15	Density, Viscosity, and Refractive Index of Binary Mixtures of Fatty Acid Ethyl Esters with Ethylcyclohexane
ρl	763.62	kg/m3	323.15	Density, Viscosity, and Refractive Index of Binary Mixtures of Fatty Acid Ethyl Esters with Ethylcyclohexane
ρl	763.60	kg/m3	323.15	Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Binary Mixtures of Ethylcyclohexane or Methylcyclohexane with n-Dodecane or n-Hexadecane at 0.1 MPa
ρl	763.59	kg/m3	323.15	Densities, Viscosities, Refractive Indices, and Surface Tensions of Binary Mixtures of 2,2,4-Trimethylpentane with Several Alkylated Cyclohexanes from (293.15 to 343.15) K
ρl	755.36	kg/m3	333.15	Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Binary Mixtures of Ethylcyclohexane or Methylcyclohexane with n-Dodecane or n-Hexadecane at 0.1 MPa
ρl	755.35	kg/m3	333.15	Densities, Viscosities, Refractive Indices, and Surface Tensions of Binary Mixtures of 2,2,4-Trimethylpentane with Several Alkylated Cyclohexanes from (293.15 to 343.15) K
ρl	747.03	kg/m3	343.15	Densities, Viscosities, Refractive Indices, and Surface Tensions of Binary Mixtures of 2,2,4-Trimethylpentane with Several Alkylated Cyclohexanes from (293.15 to 343.15) K
ΔfusS	[51.30; 51.49]	J/mol×K	[161.40; 161.84]
ΔfusS	51.30	J/mol×K	161.40	NIST
ΔfusS	51.30	J/mol×K	161.40	NIST
ΔfusS	51.49	J/mol×K	161.84	NIST
ΔfusS	51.49	J/mol×K	161.84	NIST
γ	0.03	N/m	293.20	KDB

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[116.39; 492.69]	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			9.95790e+01
Coefficient B			-7.99660e+02
Coefficient C			6.90324e+00
Coefficient D			-4.36340e-04
Coefficient E			1.14870e-07
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	116.39	J/mol×K	200.00	Calculated Property
Cp,gas	184.78	J/mol×K	344.44	Calculated Property
Cp,gas	260.63	J/mol×K	488.89	Calculated Property
Cp,gas	323.29	J/mol×K	633.33	Calculated Property
Cp,gas	371.42	J/mol×K	777.78	Calculated Property
Cp,gas	407.99	J/mol×K	922.22	Calculated Property
Cp,gas	436.16	J/mol×K	1066.67	Calculated Property
Cp,gas	458.47	J/mol×K	1211.11	Calculated Property
Cp,gas	476.84	J/mol×K	1355.56	Calculated Property
Cp,gas	492.69	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[161.03; 267.47]	J/mol×K	[160.00; 404.95]	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			1.06540e+02
Coefficient B			5.07240e+01
Coefficient C			2.46804e+00
Coefficient D			8.51930e-03
Coefficient E			-5.86790e-06
Temperature range, min.			160.00
Temperature range, max.			404.95
Cp,liquid	161.03	J/mol×K	160.00	Calculated Property
Cp,liquid	168.61	J/mol×K	187.22	Calculated Property
Cp,liquid	177.46	J/mol×K	214.43	Calculated Property
Cp,liquid	187.50	J/mol×K	241.65	Calculated Property
Cp,liquid	198.66	J/mol×K	268.87	Calculated Property
Cp,liquid	210.85	J/mol×K	296.08	Calculated Property
Cp,liquid	223.98	J/mol×K	323.30	Calculated Property
Cp,liquid	237.90	J/mol×K	350.52	Calculated Property
Cp,liquid	252.47	J/mol×K	377.73	Calculated Property
Cp,liquid	267.47	J/mol×K	404.95	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0064112; 0.0002957]	Pa×s	[200.00; 404.94]	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			-2.25310e+01
Coefficient B			1.68600e+03
Coefficient C			1.70930e+00
Coefficient D			-1.28200e-07
Coefficient E			2.00000e+00
Temperature range, min.			200.00
Temperature range, max.			404.94
η	0.0064112	Pa×s	200.00	Calculated Property
η	0.0032525	Pa×s	222.77	Calculated Property
η	0.0019013	Pa×s	245.54	Calculated Property
η	0.0012335	Pa×s	268.31	Calculated Property
η	0.0008658	Pa×s	291.08	Calculated Property
η	0.0006458	Pa×s	313.86	Calculated Property
η	0.0005052	Pa×s	336.63	Calculated Property
η	0.0004105	Pa×s	359.40	Calculated Property
η	0.0003440	Pa×s	382.17	Calculated Property
η	0.0002957	Pa×s	404.94	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[48.13; 0.00]	kJ/mol	[161.84; 609.15]	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			6.10660e+01
Coefficient B			1.10950e+00
Coefficient C			-1.64010e+00
Coefficient D			1.52320e+00
Coefficient E			-5.42560e-01
Critical temperature, Tc (K)			6.09150e+02
Temperature range, min.			161.84
Temperature range, max.			609.15
ΔvapH	48.13	kJ/mol	161.84	Calculated Property
ΔvapH	45.28	kJ/mol	211.54	Calculated Property
ΔvapH	42.59	kJ/mol	261.24	Calculated Property
ΔvapH	39.87	kJ/mol	310.94	Calculated Property
ΔvapH	36.97	kJ/mol	360.64	Calculated Property
ΔvapH	33.73	kJ/mol	410.35	Calculated Property
ΔvapH	29.96	kJ/mol	460.05	Calculated Property
ΔvapH	25.31	kJ/mol	509.75	Calculated Property
ΔvapH	18.91	kJ/mol	559.45	Calculated Property
ΔvapH	0.00	kJ/mol	609.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.64]	kPa	[291.27; 433.70]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.40223e+01
Coefficient B			-3.39182e+03
Coefficient C			-4.43220e+01
Temperature range, min.			291.27
Temperature range, max.			433.70
Pvap	1.33	kPa	291.27	Calculated Property
Pvap	3.05	kPa	307.10	Calculated Property
Pvap	6.35	kPa	322.92	Calculated Property
Pvap	12.21	kPa	338.75	Calculated Property
Pvap	21.97	kPa	354.57	Calculated Property
Pvap	37.35	kPa	370.40	Calculated Property
Pvap	60.45	kPa	386.22	Calculated Property
Pvap	93.76	kPa	402.05	Calculated Property
Pvap	140.11	kPa	417.87	Calculated Property
Pvap	202.64	kPa	433.70	Calculated Property
Pvap	[3.51e-07; 3031.84]	kPa	[161.84; 609.15]	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			7.36966e+01
Coefficient B			-7.22185e+03
Coefficient C			-8.66152e+00
Coefficient D			4.61954e-06
Coefficient E			2.00000e+00
Temperature range, min.			161.84
Temperature range, max.			609.15
Pvap	3.51e-07	kPa	161.84	Calculated Property
Pvap	1.34e-03	kPa	211.54	Calculated Property
Pvap	0.16	kPa	261.24	Calculated Property
Pvap	3.33	kPa	310.94	Calculated Property
Pvap	26.43	kPa	360.64	Calculated Property
Pvap	116.59	kPa	410.35	Calculated Property
Pvap	354.11	kPa	460.05	Calculated Property
Pvap	840.75	kPa	509.75	Calculated Property
Pvap	1690.16	kPa	559.45	Calculated Property
Pvap	3031.84	kPa	609.15	Calculated Property
Pvap	[3.59e-07; 3033.23]	kPa	[161.84; 609.15]	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			7.23704e+01
Coefficient B			-7.17302e+03
Coefficient C			-8.45462e+00
Coefficient D			4.40351e-06
Coefficient E			0.00000e+00
Temperature range, min.			161.84
Temperature range, max.			609.15
Pvap	3.59e-07	kPa	161.84	Calculated Property
Pvap	1.35e-03	kPa	211.54	Calculated Property
Pvap	0.16	kPa	261.24	Calculated Property
Pvap	3.32	kPa	310.94	Calculated Property
Pvap	26.41	kPa	360.64	Calculated Property
Pvap	116.75	kPa	410.35	Calculated Property
Pvap	355.10	kPa	460.05	Calculated Property
Pvap	843.49	kPa	509.75	Calculated Property
Pvap	1694.41	kPa	559.45	Calculated Property
Pvap	3033.23	kPa	609.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[882.45; 261.33]	kg/m3	[161.84; 609.15]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			6.93182e+01
Coefficient B			2.65250e-01
Coefficient C			6.09150e+02
Coefficient D			2.80640e-01
Temperature range, min.			161.84
Temperature range, max.			609.15
ρl	882.45	kg/m3	161.84	Calculated Property
ρl	848.22	kg/m3	211.54	Calculated Property
ρl	812.27	kg/m3	261.24	Calculated Property
ρl	774.19	kg/m3	310.94	Calculated Property
ρl	733.37	kg/m3	360.64	Calculated Property
ρl	688.84	kg/m3	410.35	Calculated Property
ρl	638.96	kg/m3	460.05	Calculated Property
ρl	580.38	kg/m3	509.75	Calculated Property
ρl	504.03	kg/m3	559.45	Calculated Property
ρl	261.33	kg/m3	609.15	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.01]	N/m	[162.15; 405.15]	Jasper (1972), surface tension of pure liquid compounds Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K
Coefficient A			5.65700e-02
Coefficient B			-1.05400e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			162.15
Temperature range, max.			405.15
γ	0.04	N/m	162.15	Calculated Property
γ	0.04	N/m	189.15	Calculated Property
γ	0.03	N/m	216.15	Calculated Property
γ	0.03	N/m	243.15	Calculated Property
γ	0.03	N/m	270.15	Calculated Property
γ	0.03	N/m	297.15	Calculated Property
γ	0.02	N/m	324.15	Calculated Property
γ	0.02	N/m	351.15	Calculated Property
γ	0.02	N/m	378.15	Calculated Property
γ	0.01	N/m	405.15	Calculated Property
γ	[0.04; 7.93e-06]	N/m	[161.84; 604.23]	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			-7.74400e-03
Coefficient B			4.02590e+01
Coefficient C			-3.24470e+00
Coefficient D			6.80100e-04
Coefficient E			-5.73190e-06
Comment			Range stopped where the equation turns negative; ChemSep gives it to 609.15 K.
Temperature range, min.			161.84
Temperature range, max.			604.23
γ	0.04	N/m	161.84	Calculated Property
γ	0.03	N/m	210.99	Calculated Property
γ	0.03	N/m	260.15	Calculated Property
γ	0.02	N/m	309.30	Calculated Property
γ	0.02	N/m	358.46	Calculated Property
γ	0.01	N/m	407.61	Calculated Property
γ	0.01	N/m	456.77	Calculated Property
γ	0.01	N/m	505.92	Calculated Property
γ	0.00	N/m	555.08	Calculated Property
γ	7.93e-06	N/m	604.23	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.09]	W/m×K	[161.84; 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			6.27510e-05
Coefficient B			1.12190e+00
Coefficient C			4.88850e+02
Coefficient D			4.56480e+04
Temperature range, min.			161.84
Temperature range, max.			1000.00
λgas	0.00	W/m×K	161.84	Calculated Property
λgas	0.01	W/m×K	254.97	Calculated Property
λgas	0.02	W/m×K	348.10	Calculated Property
λgas	0.02	W/m×K	441.23	Calculated Property
λgas	0.03	W/m×K	534.36	Calculated Property
λgas	0.05	W/m×K	627.48	Calculated Property
λgas	0.06	W/m×K	720.61	Calculated Property
λgas	0.07	W/m×K	813.74	Calculated Property
λgas	0.08	W/m×K	906.87	Calculated Property
λgas	0.09	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.14; 0.09]	W/m×K	[161.84; 404.94]	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			-4.02120e-02
Coefficient B			3.96730e+00
Coefficient C			-1.60440e+00
Coefficient D			-4.96910e-04
Coefficient E			-1.26230e-06
Temperature range, min.			161.84
Temperature range, max.			404.94
λliquid	0.14	W/m×K	161.84	Calculated Property
λliquid	0.14	W/m×K	188.85	Calculated Property
λliquid	0.13	W/m×K	215.86	Calculated Property
λliquid	0.13	W/m×K	242.87	Calculated Property
λliquid	0.12	W/m×K	269.88	Calculated Property
λliquid	0.12	W/m×K	296.90	Calculated Property
λliquid	0.11	W/m×K	323.91	Calculated Property
λliquid	0.11	W/m×K	350.92	Calculated Property
λliquid	0.10	W/m×K	377.93	Calculated Property
λliquid	0.09	W/m×K	404.94	Calculated Property

Similar Compounds

Find more compounds similar to Cyclohexane, ethyl-.

Mixtures

• Cyclohexane, ethyl- + Thiophene, tetrahydro-, 1,1-dioxide
• Cyclohexane, ethyl- + Ethanol, 2-phenoxy-
• Cyclohexane, ethyl- + Cyclohexylamine
• Cyclohexane, ethyl- + N-Formylmorpholine
• Cyclohexane, ethyl- + Water
• Cyclohexane, ethyl- + Pentane, 2,2,4-trimethyl-
• Cyclohexane, ethyl- + 1,1'-Bicyclohexyl
• Cyclohexane, ethyl- + Hexadecane
• Cyclohexane, ethyl- + Eicosane
• Cyclohexane, ethyl- + (3a«alpha»,4«beta»,7«beta»,7a«alpha»)-octahydro-4,7-methano-1H-indene
• Cyclohexane, ethyl- + Dodecane
• Decanoic acid, ethyl ester + Cyclohexane, ethyl-
• Cyclohexane, ethyl- + Dodecanoic acid, ethyl ester
• Cyclohexane, ethyl- + Tetradecanoic acid, ethyl ester
• Cyclohexane, ethyl- + 2(3H)-Furanone, dihydro-3-hydroxy-4,4-dimethyl-, (.+/-.)-

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).
• 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).
• Passut and Danner (1973), critical constants and acentric factors ChEDL chemicals 1.5.2, from Passut, C. A.; Danner, R. P. Acentric Factor. A Valuable Correlating Parameter for the Properties of Hydrocarbons. Ind. Eng. Chem. Process Des. Dev. 1973, 12, 365-368.
• 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.
• Staveley, Lobo and Calado (1981), triple points ChEDL chemicals 1.5.2, from Staveley, L. A. K.; Lobo, L. Q.; Calado, J. C. G. Triple-Points of Low Melting Substances and Their Use in Cryogenic Work. Cryogenics 1981, 21, 131-144.
• ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
• Crippen Method
• Liquid liquid equilibria for the binary systems of sulfolane with branched cycloalkanes
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• Introduction of the amine group at cycloaliphatic hydrocarbon (c-CHNH2) for the modified UNIFAC (Dortmund) model and validation in multicomponent systems containing cyclohexylamine
• Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Interactions of volatile organic compounds with the ionic liquids 1-butyl-1-methylpyrrolidinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium bis(oxalato)borate
• Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
• THERMODYNAMICS OF MIXTURES CONTAINING ALKOXYETHANOLS. XXVIII. LIQUID-LIQUID EQUILIBRIA FOR 2-PHENOXYETHANOL + SELECTED ALKANES
• Densities, Viscosities, Refractive Indices, and Surface Tensions of Binary Mixtures of 2,2,4-Trimethylpentane with Several Alkylated Cyclohexanes from (293.15 to 343.15) K
• Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Binary Mixtures of Ethylcyclohexane or Methylcyclohexane with n-Dodecane or n-Hexadecane at 0.1 MPa
• Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
• DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
• Density, Viscosity, and Refractive Index of Binary Mixtures of Fatty Acid Ethyl Esters with Ethylcyclohexane
• Thermodynamic Properties of Mixtures Containing Precursors of Vitamin B5
• Liquid-Liquid Equilibria for the Binary Systems of N-Formylmorpholine with Branched Cycloalkanes
• Critical Point Measurements for Five n-Alkylcyclohexanes (C6 to C10) by the Pulse-Heating Method
• Gas-Liquid Critical Temperatures of Some Alkenes, Amines, and Cyclic Hydrocarbons
• Solubilities of Alkylcyclohexanes in Water from 30 C to 180 C
• Apparatus for the Determination of Water Solubility in Hydrocarbon: Toluene and Alkylcyclohexanes (C6 to C8) from 30 C to 180 C
• Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
• Excess Molar Volume along with Viscosity and Refractive Index for Binary Systems of Tricyclo[5.2.1.0(2.6)]decane with Five Cycloalkanes
• Density, Viscosity, Refractive Index, and Freezing Point for Binary Mixtures of 1,1'-Bicyclohexyl with Alkylcyclohexane
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure
• Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD

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