Chemical Properties of Naphthalene, decahydro-, cis- (CAS 493-01-6)

InChI

InChI=1S/C10H18/c1-2-6-10-8-4-3-7-9(10)5-1/h9-10H,1-8H2/t9-,10+

InChI Key

NNBZCPXTIHJBJL-AOOOYVTPSA-N

Formula

C10H18

SMILES

C1CCC2CCCCC2C1

Molecular Weight¹

138.25

CAS

493-01-6

Other Names

• (Z)-Decahydronaphthalene
• Decahydronaphthalene, (Z)-
• Decahydronaphthalene, cis
• c-Decahydronaphthalene
• c-Decalin
• cis-Decahydronapthalene
• cis-bicyclo[4.4.0]decane
• cis-decahydronaphthalene
• cis-decalin
• cis-perhydronaphthalene

• 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_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 standard conditions (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).
• P_c : Critical Pressure (kPa).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ΔcH°liquid	[-6288.22; -6275.60]	kJ/mol
ΔcH°liquid	-6288.22 ± 0.92	kJ/mol	NIST
ΔcH°liquid	-6287.70 ± 1.30	kJ/mol	NIST
ΔcH°liquid	-6275.60	kJ/mol	NIST
ΔcH°liquid	-6280.90 ± 4.10	kJ/mol	NIST
ΔfH°gas	[-169.60; -169.20]	kJ/mol
ΔfH°gas	-169.20 ± 2.30	kJ/mol	NIST
ΔfH°gas	-169.60	kJ/mol	NIST
ΔfH°liquid	[-219.90; -219.50]	kJ/mol
ΔfH°liquid	-219.50 ± 0.92	kJ/mol	NIST
ΔfH°liquid	-219.90 ± 1.30	kJ/mol	NIST
ΔfusH°	9.53	kJ/mol	Joback Calculated Property
ΔsubH°	62.50	kJ/mol	NIST
ΔvapH°	[50.20; 50.30]	kJ/mol
ΔvapH°	50.20 ± 2.10	kJ/mol	NIST
ΔvapH°	50.30	kJ/mol	NIST
IE	[9.32; 9.43]	eV
IE	9.32 ± 0.05	eV	NIST
IE	9.32 ± 0.05	eV	NIST
IE	9.43 ± 0.00	eV	NIST
IE	9.40	eV	NIST
log10WS	-5.18		Relay (1.0) Calculated Property
logPoct/wat	3.367		Crippen Calculated Property
McVol	130.040	ml/mol	McGowan Calculated Property
Pc	[2490.00; 3207.00]	kPa
Pc	3200.00 ± 200.00	kPa	NIST
Pc	2490.00 ± 50.00	kPa	NIST
Pc	3207.00 ± 20.68	kPa	NIST
Inp	[1071.60; 1137.70]
Inp	1096.00		NIST
Inp	1096.00		NIST
Inp	1109.00		NIST
Inp	1130.00		NIST
Inp	1097.00		NIST
Inp	1097.00		NIST
Inp	1102.00		NIST
Inp	1090.00		NIST
Inp	1081.50		NIST
Inp	1120.00		NIST
Inp	1132.00		NIST
Inp	1087.00		NIST
Inp	1101.40		NIST
Inp	1106.20		NIST
Inp	1124.80		NIST
Inp	Outlier 1137.70		NIST
Inp	1101.40		NIST
Inp	1106.20		NIST
Inp	1100.00		NIST
Inp	1114.00		NIST
Inp	1119.00		NIST
Inp	1106.00		NIST
Inp	1085.00		NIST
Inp	1089.50		NIST
Inp	1096.10		NIST
Inp	1100.40		NIST
Inp	Outlier 1071.60		NIST
Inp	1089.50		NIST
Inp	1096.10		NIST
Inp	1100.40		NIST
Inp	1090.00		NIST
Inp	1078.85		NIST
Inp	1086.83		NIST
Inp	1092.00		NIST
Inp	1092.50		NIST
Inp	1101.09		NIST
Inp	1107.06		NIST
Inp	1085.00		NIST
Inp	1119.00		NIST
Inp	1113.00		NIST
Inp	1123.00		NIST
Inp	1101.00		NIST
Inp	1116.00		NIST
Inp	1124.00		NIST
Inp	1089.00		NIST
Inp	1093.00		NIST
Inp	1097.00		NIST
Inp	1103.00		NIST
Inp	1099.00		NIST
Inp	1097.00		NIST
Inp	1082.00		NIST
Inp	1092.00		NIST
Inp	1089.00		NIST
Inp	1119.00		NIST
Inp	1124.00		NIST
Inp	1096.00		NIST
Inp	1097.00		NIST
Inp	1132.00		NIST
Inp	Outlier 1137.70		NIST
Inp	1089.50		NIST
Inp	1096.10		NIST
Inp	1092.00		NIST
I	[1223.00; 1276.00]
I	1223.00		NIST
I	1223.00		NIST
I	1235.00		NIST
I	1276.00		NIST
I	1260.00		NIST
I	1223.00		NIST
I	1232.00		NIST
I	1227.00		NIST
I	1232.00		NIST
I	1276.00		NIST
I	1235.00		NIST
Tboil	[461.00; 469.20]	K
Tboil	466.20	K	NIST
Tboil	468.80	K	NIST
Tboil	467.75 ± 0.50	K	NIST
Tboil	465.70 ± 1.50	K	NIST
Tboil	468.85 ± 0.30	K	NIST
Tboil	468.70 ± 0.70	K	NIST
Tboil	467.80 ± 1.00	K	NIST
Tboil	469.20 ± 1.00	K	NIST
Tboil	467.80 ± 1.00	K	NIST
Tboil	Outlier 461.00 ± 3.00	K	NIST
Tboil	463.00 ± 4.00	K	NIST
Tboil	Outlier 461.00 ± 4.00	K	NIST
Tboil	466.00 ± 3.00	K	NIST
Tboil	466.00 ± 3.00	K	NIST
Tboil	466.00 ± 4.00	K	NIST
Tc	[681.00; 705.00]	K
Tc	704.00 ± 3.00	K	NIST
Tc	681.00 ± 1.50	K	NIST
Tc	705.00 ± 1.00	K	NIST
Tc	702.20 ± 1.50	K	NIST
Tfus	[222.00; 243.00]	K
Tfus	229.85 ± 0.50	K	NIST
Tfus	229.90 ± 0.50	K	NIST
Tfus	229.90 ± 0.50	K	NIST
Tfus	227.80 ± 0.30	K	NIST
Tfus	230.08 ± 0.07	K	NIST
Tfus	230.10 ± 0.05	K	NIST
Tfus	230.14 ± 0.03	K	NIST
Tfus	229.89 ± 0.40	K	NIST
Tfus	230.09 ± 0.30	K	NIST
Tfus	229.95 ± 0.60	K	NIST
Tfus	Outlier 243.00 ± 20.00	K	NIST
Tfus	229.89 ± 0.50	K	NIST
Tfus	228.00 ± 5.00	K	NIST
Tfus	222.00 ± 7.00	K	NIST
Ttriple	[230.10; 230.23]	K
Ttriple	230.12 ± 0.06	K	NIST
Ttriple	230.11 ± 0.06	K	NIST
Ttriple	230.16 ± 0.03	K	NIST
Ttriple	230.15 ± 0.10	K	NIST
Ttriple	230.23 ± 0.05	K	NIST
Ttriple	230.10 ± 0.20	K	NIST

Cheméo can also estimate Critical Volume, Standard Gibbs free energy of formation, Acentric Factor for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[236.77; 272.00]	J/mol×K	[400.00; 450.00]
Cp,gas	236.77	J/mol×K	400.00	NIST
Cp,gas	272.00	J/mol×K	450.00	NIST
Cp,liquid	[201.80; 314.40]	J/mol×K	[240.00; 420.00]
Cp,liquid	201.80	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	206.60	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	211.50	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	216.60	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	218.30	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	221.90	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	227.40	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	232.00	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	233.00	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
Cp,liquid	238.90	J/mol×K	310.00	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	244.90	J/mol×K	320.00	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	251.00	J/mol×K	330.00	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	257.40	J/mol×K	340.00	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	263.90	J/mol×K	350.00	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	270.60	J/mol×K	360.00	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	277.40	J/mol×K	370.00	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	284.50	J/mol×K	380.00	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	291.70	J/mol×K	390.00	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	299.10	J/mol×K	400.00	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	306.60	J/mol×K	410.00	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	314.40	J/mol×K	420.00	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
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	[14.43; 14.43]	kJ/mol	[242.80; 242.80]
ΔfusH	14.43	kJ/mol	242.80	NIST
ΔfusH	14.43	kJ/mol	242.80	NIST
ΔsubH	64.80	kJ/mol	230.00	NIST
ΔvapH	45.50	kJ/mol	422.00	NIST
ρl	[874.05; 896.85]	kg/m3	[293.15; 323.15]
ρl	896.85	kg/m3	293.15	Excess Molar Volume along with Viscosity, Flash Point, and Refractive Index for Binary Mixtures of cis-Decalin or trans-Decalin with C9 to C11 n-Alkanes
ρl	893.06	kg/m3	298.15	Excess Molar Volume along with Viscosity, Flash Point, and Refractive Index for Binary Mixtures of cis-Decalin or trans-Decalin with C9 to C11 n-Alkanes
ρl	889.26	kg/m3	303.15	Excess Molar Volume along with Viscosity, Flash Point, and Refractive Index for Binary Mixtures of cis-Decalin or trans-Decalin with C9 to C11 n-Alkanes
ρl	885.46	kg/m3	308.15	Excess Molar Volume along with Viscosity, Flash Point, and Refractive Index for Binary Mixtures of cis-Decalin or trans-Decalin with C9 to C11 n-Alkanes
ρl	881.65	kg/m3	313.15	Excess Molar Volume along with Viscosity, Flash Point, and Refractive Index for Binary Mixtures of cis-Decalin or trans-Decalin with C9 to C11 n-Alkanes
ρl	877.85	kg/m3	318.15	Excess Molar Volume along with Viscosity, Flash Point, and Refractive Index for Binary Mixtures of cis-Decalin or trans-Decalin with C9 to C11 n-Alkanes
ρl	874.05	kg/m3	323.15	Excess Molar Volume along with Viscosity, Flash Point, and Refractive Index for Binary Mixtures of cis-Decalin or trans-Decalin with C9 to C11 n-Alkanes

Datasets

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
303.15	100.00	888.5
303.15	5000.00	891.4
303.15	10000.00	894.4
303.15	15000.00	897.3
303.15	20000.00	899.9
303.15	25000.00	902.8
303.15	30000.00	905.5
303.15	35000.00	908.0
303.15	40000.00	910.6
303.15	45000.00	913.0
303.15	50000.00	915.3
303.15	55000.00	917.6
303.15	60000.00	919.9
303.15	65000.00	922.1
323.15	100.00	873.2
323.15	5000.00	876.5
323.15	10000.00	879.8
323.15	15000.00	883.0
323.15	20000.00	886.0
323.15	25000.00	889.0
323.15	30000.00	891.8
323.15	35000.00	894.6
323.15	40000.00	897.3
323.15	45000.00	899.9
323.15	50000.00	902.4
323.15	55000.00	904.8
323.15	60000.00	907.3
323.15	65000.00	909.6
343.15	100.00	857.8
343.15	5000.00	861.5
343.15	10000.00	865.1
343.15	15000.00	868.6
343.15	20000.00	871.9
343.15	25000.00	875.1
343.15	30000.00	878.3
343.15	35000.00	881.2
343.15	40000.00	884.1
343.15	45000.00	887.0
343.15	50000.00	889.7
343.15	55000.00	892.3
343.15	60000.00	894.9
343.15	65000.00	897.4
Reference

Similar Compounds

Find more compounds similar to Naphthalene, decahydro-, cis-.

Mixtures

• Naphthalene, decahydro-, cis- + Naphthalene, decahydro-, trans- + Dibenzothiophene
• Carbon dioxide + Naphthalene, decahydro-, cis-
• Naphthalene, decahydro-, cis- + Naphthalene, decahydro-, trans-
• Naphthalene, decahydro-, cis- + Naphthalene, decahydro-, trans- + Decane
• Naphthalene, decahydro-, cis- + Hexadecane + Naphthalene, decahydro-, trans-
• Naphthalene, decahydro-, cis- + Naphthalene, 1,2,3,4-tetrahydro- + Naphthalene, decahydro-, trans-
• Naphthalene, decahydro-, cis- + Naphthalene, decahydro-, trans- + Cyclohexane
• Toluene + Naphthalene, decahydro-, cis- + Naphthalene, decahydro-, trans-
• Naphthalene, decahydro-, cis- + Nonane, 2,2,4,4,6,8,8-heptamethyl- + Cyclohexane, methyl-
• Naphthalene, decahydro-, cis- + Nonane
• Naphthalene, decahydro-, cis- + Decane
• Undecane + Naphthalene, decahydro-, cis-
• Naphthalene, decahydro-, cis- + Naphthalene, decahydro-, trans- + Naphthalene
• Naphthalene, decahydro-, cis- + Naphthalene, decahydro-, trans- + Water
• Naphthalene, decahydro-, cis- + 1,2-Ethanediol + Naphthalene, decahydro-, trans-
• Naphthalene, decahydro-, cis- + Naphthalene, decahydro-, trans- + Cyclohexane, methyl-
• Cyclopentanol + Naphthalene, decahydro-, cis- + Naphthalene, decahydro-, trans-

Sources

• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
• Stereoisomeric effects on volumetric properties under pressure for the system cis- + trans-decalin
• High-pressure phase behaviour of the binary system {CO2 + cis-decalin} from (292.75 to 373.75) K
• High pressure speed of sound and density of (decalin + n-decane), (decalin + n-hexadecane) and (n-decane + n-hexadecane) systems and thermodynamic modeling with PHCT equation of state
• Solubility of dibenzothiophene in nine organic solvents: Experimental measurement and thermodynamic modelling
• Speeds of Sound and Densities of Ternary and Quaternary Mixtures of Tetralin, Decalin, n-Decane, and n-Hexadecane: Experiments and Thermodynamic Modeling with PC-SAFT Equation of State
• Densities and Viscosities for the Ternary System of Decalin + Methylcyclohexane + Cyclopentanol and Corresponding Binaries at T = 293.15 to 343.15 K
• Thermodynamic Studies of Solubility for Naphthalene in 12 Solvents from 279 to 330 K
• High-Pressure Viscosity and Density Measurements of the Ternary System Methylcyclohexane + cis-Decalin + 2,2,4,4,6,8,8-Heptamethylnonane
• Excess Molar Volume along with Viscosity, Flash Point, and Refractive Index for Binary Mixtures of cis-Decalin or trans-Decalin with C9 to C11 n-Alkanes
• Liquid Liquid Equilibria at Three Temperatures (between 280.15 K and 333.15 K) of Binary, Ternary, and Quaternary Systems Involving Monoethylene Glycol, Water, Cyclohexane, para-Xylene, trans- and cis-Dimethylcyclohexane, and trans- and cis-Decahydronaphthalene
• Density and Viscosity of Decalin, Cyclohexane, and Toluene Binary Mixtures at (283.15, 293.15, 303.15, 313.15, and 323.15) K
• Joback Method
• McGowan Method
• NIST Webbook
• 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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