Chemical Properties of Naphthalene, decahydro- (CAS 91-17-8)

InChI

InChI=1S/C10H18/c1-2-6-10-8-4-3-7-9(10)5-1/h9-10H,1-8H2

InChI Key

NNBZCPXTIHJBJL-UHFFFAOYSA-N

Formula

C10H18

SMILES

C1CCC2CCCCC2C1

Molecular Weight¹

138.25

CAS

91-17-8

Other Names

• Bicyclo[4.4.0]decane
• Cis-decahydronaphthalene
• Dec
• Decahydronaphthalene
• Decalin
• Decaline
• Decanhydronaphthalene
• Dekalin
• Dekalina
• NSC 406139
• Naphthalane
• Naphthan
• Naphthane
• Perhydronaphthalene
• UN 1147

• 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).
• 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_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).
• 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).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• 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).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ΔcH°liquid	-6226.52	kJ/mol	NIST
ΔfG°	106.42	kJ/mol	Joback Calculated Property
ΔfH°gas	-128.77	kJ/mol	Joback Calculated Property
ΔfusH°	9.53	kJ/mol	Joback Calculated Property
ΔvapH°	38.37	kJ/mol	Joback Calculated Property
IE	[9.14; 9.35]	eV
IE	9.14	eV	NIST
IE	9.35	eV	NIST
log10WS	-5.19		Estimat...
logPoct/wat	3.367		Crippen Calculated Property
McVol	130.040	ml/mol	McGowan Calculated Property
Pc	2080.00 ± 151.99	kPa	NIST
Inp	[173.01; 1089.00]
Inp	1042.00		NIST
Inp	1054.00		NIST
Inp	1066.00		NIST
Inp	1063.00		NIST
Inp	1056.00		NIST
Inp	1089.00		NIST
Inp	1055.00		NIST
Inp	1054.00		NIST
Inp	1087.00		NIST
Inp	1064.00		NIST
Inp	1043.00		NIST
Inp	Outlier 173.01		NIST
Inp	Outlier 173.31		NIST
Inp	1055.00		NIST
Inp	1089.00		NIST
Inp	Outlier 173.01		NIST
S°liquid	265.01	J/mol×K	NIST
Tboil	[445.00; 465.00]	K
Tboil	464.25	K	Excess ...
Tboil	463.20	K	NIST
Tboil	465.00 ± 5.00	K	NIST
Tboil	465.00 ± 2.00	K	NIST
Tboil	Outlier 445.00 ± 10.00	K	NIST
Tboil	461.00 ± 6.00	K	NIST
Tc	645.00 ± 2.00	K	NIST
Tfus	149.00 ± 2.50	K	NIST
Vc	0.477	m3/kmol	Joback Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[286.16; 401.24]	J/mol×K	[458.76; 680.81]
Cp,gas	286.16	J/mol×K	458.76	Joback Calculated Property
Cp,gas	308.56	J/mol×K	495.77	Joback Calculated Property
Cp,gas	329.59	J/mol×K	532.78	Joback Calculated Property
Cp,gas	349.32	J/mol×K	569.78	Joback Calculated Property
Cp,gas	367.80	J/mol×K	606.79	Joback Calculated Property
Cp,gas	385.09	J/mol×K	643.80	Joback Calculated Property
Cp,gas	401.24	J/mol×K	680.81	Joback Calculated Property
Cp,liquid	[219.20; 251.00]	J/mol×K	[298.00; 313.00]
Cp,liquid	233.51	J/mol×K	298.00	NIST
Cp,liquid	232.20	J/mol×K	298.15	NIST
Cp,liquid	232.20	J/mol×K	298.15	NIST
Cp,liquid	232.00	J/mol×K	298.15	NIST
Cp,liquid	232.08	J/mol×K	298.15	NIST
Cp,liquid	220.06	J/mol×K	298.15	NIST
Cp,liquid	219.20	J/mol×K	311.00	NIST
Cp,liquid	251.00	J/mol×K	313.00	NIST
η	[0.0004040; 0.0046703]	Pa×s	[224.26; 458.76]
η	0.0046703	Pa×s	224.26	Joback Calculated Property
η	0.0022946	Pa×s	263.34	Joback Calculated Property
η	0.0013547	Pa×s	302.43	Joback Calculated Property
η	0.0009023	Pa×s	341.51	Joback Calculated Property
η	0.0006533	Pa×s	380.59	Joback Calculated Property
η	0.0005024	Pa×s	419.68	Joback Calculated Property
η	0.0004040	Pa×s	458.76	Joback Calculated Property
ΔfusH	[2.21; 14.41]	kJ/mol	[230.10; 242.78]
ΔfusH	2.21	kJ/mol	230.10	NIST
ΔfusH	14.41	kJ/mol	242.78	NIST
ρl	[826.61; 880.46]	kg/m3	[293.15; 363.15]
ρl	880.46	kg/m3	293.15	Density...
ρl	876.72	kg/m3	298.15	Density...
ρl	872.96	kg/m3	303.15	Density...
ρl	865.43	kg/m3	313.15	Density...
ρl	857.01	kg/m3	323.15	Density...
ρl	849.45	kg/m3	333.15	Density...
ρl	841.87	kg/m3	343.15	Density...
ρl	834.26	kg/m3	353.15	Density...
ρl	826.61	kg/m3	363.15	Density...
ΔfusS	[9.60; 59.37]	J/mol×K	[230.10; 242.78]
ΔfusS	9.60	J/mol×K	230.10	NIST
ΔfusS	59.37	J/mol×K	242.78	NIST

Similar Compounds

Find more compounds similar to Naphthalene, decahydro-.

Mixtures

• Diisopropyl ether + Naphthalene, decahydro-
• Naphthalene, decahydro- + Adamantane, 1,3-dimethyl-
• Hexatriacontane + Naphthalene, decahydro-
• Naphthalene, 1-methyl- + Hexatriacontane + Naphthalene, decahydro-
• Hexatriacontane + Naphthalene, decahydro- + Diethyl disulfide
• Naphthalene, decahydro- + Water
• Carbon dioxide + Naphthalene, decahydro- + Water
• Propane + Naphthalene, decahydro-

Sources

• Crippen Method
• Experimental solubility data of various n-alkane waxes: effects of alkane chain length, alkane odd versus even carbon number structures, and solvent chemistry on solubility
• Measurement and correlation of phase equilibria for (water + aromatic hydrocarbon) binary mixtures at T = (573 to 623) K using microfluidic mixing
• Effect of water content on the equilibrium pressure of (carbon dioxide + decane and + decalin) from T = (313.15 to 333.15) K
• Excess volumes, densities, speeds of sound and viscosities for the binary systems of diisopropyl ether with hydrocarbons at 303.15K
• High -Pressure Phase Diagrams of Propane + Decahydronaphthalene and Propane + Naphthalene Mixtures
• Density, Viscosity, Surface Tension, and Refractive Index for Binary Mixtures of 1,3-Dimethyladamantane with Four C10 Alkanes
• Joback Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook

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Outlier This icon means that the value is more than 2 standard deviations away from the property mean.