Chemical Properties of Cyclohexane, decyl- (CAS 1795-16-0)

InChI

InChI=1S/C16H32/c1-2-3-4-5-6-7-8-10-13-16-14-11-9-12-15-16/h16H,2-15H2,1H3

InChI Key

STWFZICHPLEOIC-UHFFFAOYSA-N

Formula

C16H32

SMILES

CCCCCCCCCCC1CCCCC1

Molecular Weight¹

224.43

CAS

1795-16-0

Other Names

• 1-Decylcyclohexane
• 1-cyclohexyldecane
• Cyclohexane, n-decyl-
• Decane, 1-cyclohexyl-
• decylcyclohexane
• n-decylcyclohexane

• ω : Acentric Factor.
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_sat : Molar heat capacity at saturation pressure (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_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).
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• S°_gas : 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).
• T_fus : Normal melting (fusion) point (K).
• T_fus : Melting point (K).
• T_triple : Triple Point Temperature (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	0.6130		KDB
ΔcH°liquid	[-10532.80; -10451.10]	kJ/mol
ΔcH°liquid	-10451.10 ± 3.30	kJ/mol	NIST
ΔcH°liquid	-10451.20 ± 1.80	kJ/mol	NIST
ΔcH°liquid	-10532.80 ± 2.20	kJ/mol	NIST
ΔfG°	108.29	kJ/mol	Joback Calculated Property
ΔfH°gas	-336.90 ± 2.40	kJ/mol	NIST
ΔfH°liquid	-418.40 ± 2.10	kJ/mol	NIST
ΔfusH°	29.03	kJ/mol	Joback Calculated Property
ΔvapH°	[78.70; 79.70]	kJ/mol
ΔvapH°	78.70 ± 0.80	kJ/mol	NIST
ΔvapH°	79.70	kJ/mol	NIST
ΔvapH°	78.76	kJ/mol	NIST
IE	9.76	eV	Relay (1.0) Calculated Property
log10WS	-7.31		Relay (1.0) Calculated Property
logPoct/wat	6.098		Crippen Calculated Property
McVol	225.440	ml/mol	McGowan Calculated Property
Pc	1540.00	kPa	KDB
Inp	[1638.00; 1679.00]
Inp	1658.00		NIST
Inp	Outlier 1679.00		NIST
Inp	1638.00		NIST
Inp	1640.00		NIST
Inp	1642.00		NIST
Inp	1656.00		NIST
Inp	1656.20		NIST
Inp	1655.90		NIST
Inp	1650.70		NIST
Inp	1656.20		NIST
Inp	1658.40		NIST
Inp	1650.70		NIST
Inp	1656.20		NIST
Inp	1658.40		NIST
Inp	1656.20		NIST
Inp	1655.90		NIST
Inp	1648.54		NIST
Inp	1653.53		NIST
Inp	1656.86		NIST
Inp	1655.41		NIST
Inp	1660.95		NIST
Inp	1664.11		NIST
Inp	1640.00		NIST
S°gas	694.42	J/mol×K	NIST
Tboil	[560.00; 570.80]	K
Tboil	570.80	K	KDB
Tboil	560.00 ± 3.00	K	NIST
Tc	750.00	K	KDB
Tfus	[271.00; 271.45]	K
Tfus	271.00	K	KDB
Tfus	271.45 ± 0.50	K	NIST
Tfus	271.40 ± 0.04	K	NIST
Tfus	271.40 ± 0.04	K	NIST
Tfus	271.43 ± 0.03	K	NIST
Tfus	271.14 ± 0.40	K	NIST
Ttriple	[271.42; 271.44]	K
Ttriple	271.43 ± 0.02	K	NIST
Ttriple	271.42 ± 0.05	K	NIST
Ttriple	271.44 ± 0.02	K	NIST
Vc	0.865	m3/kmol	KDB
Zc	0.2134950		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Csat	[439.10; 453.50]	J/mol×K	[280.00; 300.00]
Csat	439.10	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
Csat	446.30	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
Csat	452.10	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
Csat	453.50	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	[38.62; 38.62]	kJ/mol	[271.40; 271.40]
ΔfusH	38.62	kJ/mol	271.40	NIST
ΔfusH	38.62	kJ/mol	271.40	NIST
ΔvapH	[50.38; 76.70]	kJ/mol	[398.00; 570.80]
ΔvapH	76.70	kJ/mol	398.00	NIST
ΔvapH	61.60	kJ/mol	520.00	NIST
ΔvapH	50.38	kJ/mol	570.80	KDB
ρl	[764.40; 821.93]	kg/m3	[288.15; 373.15]
ρl	821.93	kg/m3	288.15	Thermophysical Properties of Binary Mixtures of n-Dodecane with n-Alkylcyclohexanes: Experimental Measurements and Molecular Dynamics Simulations
ρl	819.00	kg/m3	293.00	KDB
ρl	818.55	kg/m3	293.15	Densities, Speeds of Sound, and Viscosities of Binary Mixtures of an n-Alkylcyclohexane (n-Propyl-, n-Pentyl-, n-Hexyl-, n-Heptyl, n-Octyl-, n-Nonyl-, n-Decyl-, and n-Dodecyl-) with n-Hexadecane
ρl	818.54	kg/m3	293.15	Thermophysical Properties of Binary Mixtures of n-Dodecane with n-Alkylcyclohexanes: Experimental Measurements and Molecular Dynamics Simulations
ρl	815.16	kg/m3	298.15	Thermophysical Properties of Binary Mixtures of n-Dodecane with n-Alkylcyclohexanes: Experimental Measurements and Molecular Dynamics Simulations
ρl	811.78	kg/m3	303.15	Densities, Speeds of Sound, and Viscosities of Binary Mixtures of an n-Alkylcyclohexane (n-Propyl-, n-Pentyl-, n-Hexyl-, n-Heptyl, n-Octyl-, n-Nonyl-, n-Decyl-, and n-Dodecyl-) with n-Hexadecane
ρl	811.78	kg/m3	303.15	Thermophysical Properties of Binary Mixtures of n-Dodecane with n-Alkylcyclohexanes: Experimental Measurements and Molecular Dynamics Simulations
ρl	805.02	kg/m3	313.15	Densities, Speeds of Sound, and Viscosities of Binary Mixtures of an n-Alkylcyclohexane (n-Propyl-, n-Pentyl-, n-Hexyl-, n-Heptyl, n-Octyl-, n-Nonyl-, n-Decyl-, and n-Dodecyl-) with n-Hexadecane
ρl	805.02	kg/m3	313.15	Thermophysical Properties of Binary Mixtures of n-Dodecane with n-Alkylcyclohexanes: Experimental Measurements and Molecular Dynamics Simulations
ρl	798.27	kg/m3	323.15	Densities, Speeds of Sound, and Viscosities of Binary Mixtures of an n-Alkylcyclohexane (n-Propyl-, n-Pentyl-, n-Hexyl-, n-Heptyl, n-Octyl-, n-Nonyl-, n-Decyl-, and n-Dodecyl-) with n-Hexadecane
ρl	798.26	kg/m3	323.15	Thermophysical Properties of Binary Mixtures of n-Dodecane with n-Alkylcyclohexanes: Experimental Measurements and Molecular Dynamics Simulations
ρl	791.50	kg/m3	333.15	Densities, Speeds of Sound, and Viscosities of Binary Mixtures of an n-Alkylcyclohexane (n-Propyl-, n-Pentyl-, n-Hexyl-, n-Heptyl, n-Octyl-, n-Nonyl-, n-Decyl-, and n-Dodecyl-) with n-Hexadecane
ρl	791.49	kg/m3	333.15	Thermophysical Properties of Binary Mixtures of n-Dodecane with n-Alkylcyclohexanes: Experimental Measurements and Molecular Dynamics Simulations
ρl	784.80	kg/m3	343.15	Densities, Speeds of Sound, and Viscosities of Binary Mixtures of an n-Alkylcyclohexane (n-Propyl-, n-Pentyl-, n-Hexyl-, n-Heptyl, n-Octyl-, n-Nonyl-, n-Decyl-, and n-Dodecyl-) with n-Hexadecane
ρl	778.00	kg/m3	353.15	Densities, Speeds of Sound, and Viscosities of Binary Mixtures of an n-Alkylcyclohexane (n-Propyl-, n-Pentyl-, n-Hexyl-, n-Heptyl, n-Octyl-, n-Nonyl-, n-Decyl-, and n-Dodecyl-) with n-Hexadecane
ρl	771.20	kg/m3	363.15	Densities, Speeds of Sound, and Viscosities of Binary Mixtures of an n-Alkylcyclohexane (n-Propyl-, n-Pentyl-, n-Hexyl-, n-Heptyl, n-Octyl-, n-Nonyl-, n-Decyl-, and n-Dodecyl-) with n-Hexadecane
ρl	764.40	kg/m3	373.15	Densities, Speeds of Sound, and Viscosities of Binary Mixtures of an n-Alkylcyclohexane (n-Propyl-, n-Pentyl-, n-Hexyl-, n-Heptyl, n-Octyl-, n-Nonyl-, n-Decyl-, and n-Dodecyl-) with n-Hexadecane
γ	0.03	N/m	298.20	KDB

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tfus	[271.30; 293.90]	K	[100.00; 100100.00]
Tfus	271.30	K	100.00	Solid-Liquid Equilibria under High Pressure of Eight Pure n-Alkylcyclohexanes
Tfus	276.00	K	20000.00	Solid-Liquid Equilibria under High Pressure of Eight Pure n-Alkylcyclohexanes
Tfus	280.50	K	40100.00	Solid-Liquid Equilibria under High Pressure of Eight Pure n-Alkylcyclohexanes
Tfus	284.80	K	59900.00	Solid-Liquid Equilibria under High Pressure of Eight Pure n-Alkylcyclohexanes
Tfus	289.20	K	80100.00	Solid-Liquid Equilibria under High Pressure of Eight Pure n-Alkylcyclohexanes
Tfus	293.90	K	100100.00	Solid-Liquid Equilibria under High Pressure of Eight Pure n-Alkylcyclohexanes

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[306.78; 829.86]	J/mol×K	[273.00; 1000.00]	Joback Predicted correlation
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K
Coefficient A			-7.72610e+01
Coefficient B			1.64592e+00
Coefficient C			-9.27600e-04
Coefficient D			1.88800e-07
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	306.78	J/mol×K	273.00	Calculated Property
Cp,gas	397.29	J/mol×K	353.78	Calculated Property
Cp,gas	478.31	J/mol×K	434.56	Calculated Property
Cp,gas	550.43	J/mol×K	515.33	Calculated Property
Cp,gas	614.26	J/mol×K	596.11	Calculated Property
Cp,gas	670.39	J/mol×K	676.89	Calculated Property
Cp,gas	719.42	J/mol×K	757.67	Calculated Property
Cp,gas	761.94	J/mol×K	838.44	Calculated Property
Cp,gas	798.56	J/mol×K	919.22	Calculated Property
Cp,gas	829.86	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0075812; 0.0002388]	Pa×s	[271.30; 525.00]	Joback Predicted correlation
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-1.20374e+01
Coefficient B			1.94127e+03
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			271.30
Temperature range, max.			525.00
η	0.0075812	Pa×s	271.30	Calculated Property
η	0.0038659	Pa×s	299.49	Calculated Property
η	0.0022136	Pa×s	327.68	Calculated Property
η	0.0013845	Pa×s	355.87	Calculated Property
η	0.0009277	Pa×s	384.06	Calculated Property
η	0.0006566	Pa×s	412.25	Calculated Property
η	0.0004858	Pa×s	440.43	Calculated Property
η	0.0003726	Pa×s	468.62	Calculated Property
η	0.0002946	Pa×s	496.81	Calculated Property
η	0.0002388	Pa×s	525.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.64]	kPa	[427.81; 591.43]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.56565e+01
Coefficient B			-5.17811e+03
Coefficient C			-9.08880e+01
Temperature range, min.			427.81
Temperature range, max.			591.43
Pvap	1.33	kPa	427.81	Calculated Property
Pvap	2.93	kPa	445.99	Calculated Property
Pvap	5.96	kPa	464.17	Calculated Property
Pvap	11.35	kPa	482.35	Calculated Property
Pvap	20.41	kPa	500.53	Calculated Property
Pvap	34.92	kPa	518.71	Calculated Property
Pvap	57.19	kPa	536.89	Calculated Property
Pvap	90.12	kPa	555.07	Calculated Property
Pvap	137.22	kPa	573.25	Calculated Property
Pvap	202.64	kPa	591.43	Calculated Property
Pvap	[4.71e-06; 1704.43]	kPa	[271.42; 751.25]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			1.83202e+02
Coefficient B			-1.66574e+04
Coefficient C			-2.40646e+01
Coefficient D			1.02076e-05
Coefficient E			0.00000e+00
Temperature range, min.			271.42
Temperature range, max.			751.25
Pvap	4.71e-06	kPa	271.42	Calculated Property
Pvap	2.07e-03	kPa	324.73	Calculated Property
Pvap	0.11	kPa	378.05	Calculated Property
Pvap	1.63	kPa	431.36	Calculated Property
Pvap	11.35	kPa	484.68	Calculated Property
Pvap	48.44	kPa	537.99	Calculated Property
Pvap	150.31	kPa	591.31	Calculated Property
Pvap	379.07	kPa	644.62	Calculated Property
Pvap	837.15	kPa	697.94	Calculated Property
Pvap	1704.43	kPa	751.25	Calculated Property
Pvap	[6.94; 101.17]	kPa	[469.96; 570.66]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.41750e+01
Coefficient B			-4.39625e+03
Coefficient C			-1.10713e+02
Reference			Camin, Forziati, et al., 1954
Temperature range, min.			469.96
Temperature range, max.			570.66
Pvap	6.94	kPa	469.96	Calculated Property
Pvap	10.05	kPa	481.15	Calculated Property
Pvap	14.23	kPa	492.34	Calculated Property
Pvap	19.75	kPa	503.53	Calculated Property
Pvap	26.93	kPa	514.72	Calculated Property
Pvap	36.11	kPa	525.90	Calculated Property
Pvap	47.67	kPa	537.09	Calculated Property
Pvap	62.05	kPa	548.28	Calculated Property
Pvap	79.72	kPa	559.47	Calculated Property
Pvap	101.17	kPa	570.66	Calculated Property

Similar Compounds

Find more compounds similar to Cyclohexane, decyl-.

Mixtures

• Cyclohexane, decyl- + Dodecane
• Cyclohexane, decyl- + Hexadecane

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• Densities, Speeds of Sound, and Viscosities of Binary Mixtures of an n-Alkylcyclohexane (n-Propyl-, n-Pentyl-, n-Hexyl-, n-Heptyl, n-Octyl-, n-Nonyl-, n-Decyl-, and n-Dodecyl-) with n-Hexadecane
• Thermophysical Properties of Binary Mixtures of n-Dodecane with n-Alkylcyclohexanes: Experimental Measurements and Molecular Dynamics Simulations
• Solid-Liquid Equilibria under High Pressure of Eight Pure n-Alkylcyclohexanes
• Joback Method
• KDB
• 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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