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

• ω : Acentric Factor.
• 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_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).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I_p : Polar retention indices.
• 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.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.2321; 0.2942]
ω	0.2849		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.2321		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.2942		ChemSep v8.3 pure component data Compiled value
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
μ	0.00	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	85.52	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	[-169.60; -169.20]	kJ/mol
ΔfH°gas	-169.24	kJ/mol	ChemSep v8.3 pure component data Compiled value
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; 3242.40]	kPa
Pc	3200.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value
Pc	3201.87	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	3150.90	kPa	Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc	3242.40	kPa	ChemSep v8.3 pure component data Compiled value
Pc	3200.00 ± 200.00	kPa	NIST
Pc	Outlier 2490.00 ± 50.00	kPa	NIST
Pc	3207.00 ± 20.68	kPa	NIST
Ptriple	1.57e-04	kPa	ChemSep v8.3 pure component data Compiled value
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
Ip	[1223.00; 1276.00]
Ip	1223.00		NIST
Ip	1223.00		NIST
Ip	1235.00		NIST
Ip	1276.00		NIST
Ip	1260.00		NIST
Ip	1223.00		NIST
Ip	1232.00		NIST
Ip	1227.00		NIST
Ip	1232.00		NIST
Ip	1276.00		NIST
Ip	1235.00		NIST
Tboil	[461.00; 469.20]	K
Tboil	468.96	K	ChemSep v8.3 pure component data Compiled value
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; 705.26]	K
Tc	703.60	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value
Tc	702.30	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	705.26	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	702.25	K	ChemSep v8.3 pure component data Compiled value
Tc	704.00 ± 3.00	K	NIST
Tc	Outlier 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	230.20	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	230.17	K	ChemSep v8.3 pure component data Compiled value
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	Outlier 222.00 ± 7.00	K	NIST
Ttriple	[230.10; 230.23]	K
Ttriple	230.20	K	ChemSep v8.3 pure component data Compiled value
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
UQi	4.78		ChemSep v8.3 pure component data Compiled value
URi	6.29		ChemSep v8.3 pure component data Compiled value
Vc	[0.480; 0.485]	m3/kmol
Vc	0.485	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.480	m3/kmol	ChemSep v8.3 pure component data Compiled value
Zc	0.2670000		ChemSep v8.3 pure component data Compiled value
Zra	0.26		ChemSep v8.3 pure component data Compiled value

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
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

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[112.74; 570.44]	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			9.09230e+01
Coefficient B			-7.88660e+02
Coefficient C			7.11324e+00
Coefficient D			-4.61710e-04
Coefficient E			1.23500e-07
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	112.74	J/mol×K	200.00	Calculated Property
Cp,gas	198.61	J/mol×K	344.44	Calculated Property
Cp,gas	292.04	J/mol×K	488.89	Calculated Property
Cp,gas	368.23	J/mol×K	633.33	Calculated Property
Cp,gas	426.17	J/mol×K	777.78	Calculated Property
Cp,gas	469.84	J/mol×K	922.22	Calculated Property
Cp,gas	503.28	J/mol×K	1066.67	Calculated Property
Cp,gas	529.71	J/mol×K	1211.11	Calculated Property
Cp,gas	551.51	J/mol×K	1355.56	Calculated Property
Cp,gas	570.44	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[198.65; 428.77]	J/mol×K	[230.20; 600.00]	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			2.28750e+01
Coefficient B			1.83220e+02
Coefficient C			2.81134e+00
Coefficient D			8.01130e-03
Coefficient E			-5.32610e-06
Temperature range, min.			230.20
Temperature range, max.			600.00
Cp,liquid	198.65	J/mol×K	230.20	Calculated Property
Cp,liquid	216.92	J/mol×K	271.29	Calculated Property
Cp,liquid	240.05	J/mol×K	312.38	Calculated Property
Cp,liquid	266.59	J/mol×K	353.47	Calculated Property
Cp,liquid	295.33	J/mol×K	394.56	Calculated Property
Cp,liquid	325.10	J/mol×K	435.64	Calculated Property
Cp,liquid	354.64	J/mol×K	476.73	Calculated Property
Cp,liquid	382.64	J/mol×K	517.82	Calculated Property
Cp,liquid	407.78	J/mol×K	558.91	Calculated Property
Cp,liquid	428.77	J/mol×K	600.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0155684; 0.0001920]	Pa×s	[243.15; 561.80]	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			-1.02870e+02
Coefficient B			5.38790e+03
Coefficient C			1.40860e+01
Coefficient D			-1.41270e-05
Coefficient E			2.00000e+00
Temperature range, min.			243.15
Temperature range, max.			561.80
η	0.0155684	Pa×s	243.15	Calculated Property
η	0.0048679	Pa×s	278.56	Calculated Property
η	0.0022045	Pa×s	313.96	Calculated Property
η	0.0012519	Pa×s	349.37	Calculated Property
η	0.0008172	Pa×s	384.77	Calculated Property
η	0.0005802	Pa×s	420.18	Calculated Property
η	0.0004319	Pa×s	455.58	Calculated Property
η	0.0003291	Pa×s	490.99	Calculated Property
η	0.0002522	Pa×s	526.39	Calculated Property
η	0.0001920	Pa×s	561.80	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[55.70; 0.00]	kJ/mol	[230.20; 702.25]	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			7.89381e+01
Coefficient B			1.12005e+00
Coefficient C			-5.90284e-01
Coefficient D			-6.48808e-01
Coefficient E			6.01197e-01
Critical temperature, Tc (K)			7.02250e+02
Temperature range, min.			230.20
Temperature range, max.			702.25
ΔvapH	55.70	kJ/mol	230.20	Calculated Property
ΔvapH	51.84	kJ/mol	282.65	Calculated Property
ΔvapH	48.35	kJ/mol	335.10	Calculated Property
ΔvapH	45.09	kJ/mol	387.55	Calculated Property
ΔvapH	41.89	kJ/mol	440.00	Calculated Property
ΔvapH	38.50	kJ/mol	492.45	Calculated Property
ΔvapH	34.56	kJ/mol	544.90	Calculated Property
ΔvapH	29.45	kJ/mol	597.35	Calculated Property
ΔvapH	21.88	kJ/mol	649.80	Calculated Property
ΔvapH	0.00	kJ/mol	702.25	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.63e-04; 3241.62]	kPa	[230.20; 702.25]	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			1.26602e+02
Coefficient B			-1.06710e+04
Coefficient C			-1.64460e+01
Coefficient D			9.06180e-06
Coefficient E			2.00000e+00
Temperature range, min.			230.20
Temperature range, max.			702.25
Pvap	1.63e-04	kPa	230.20	Calculated Property
Pvap	0.04	kPa	282.65	Calculated Property
Pvap	1.16	kPa	335.10	Calculated Property
Pvap	11.17	kPa	387.55	Calculated Property
Pvap	54.67	kPa	440.00	Calculated Property
Pvap	176.86	kPa	492.45	Calculated Property
Pvap	441.30	kPa	544.90	Calculated Property
Pvap	935.17	kPa	597.35	Calculated Property
Pvap	1792.38	kPa	649.80	Calculated Property
Pvap	3241.62	kPa	702.25	Calculated Property
Pvap	[5.53; 102.74]	kPa	[373.03; 469.53]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.38166e+01
Coefficient B			-3.67190e+03
Coefficient C			-6.97310e+01
Reference			Camin and Rossini, 1955
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			373.03
Temperature range, max.			469.53
Pvap	5.53	kPa	373.03	Calculated Property
Pvap	8.36	kPa	383.75	Calculated Property
Pvap	12.30	kPa	394.47	Calculated Property
Pvap	17.65	kPa	405.20	Calculated Property
Pvap	24.78	kPa	415.92	Calculated Property
Pvap	34.07	kPa	426.64	Calculated Property
Pvap	46.00	kPa	437.36	Calculated Property
Pvap	61.05	kPa	448.09	Calculated Property
Pvap	79.77	kPa	458.81	Calculated Property
Pvap	102.74	kPa	469.53	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[941.47; 288.99]	kg/m3	[230.20; 702.25]	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			7.69084e+01
Coefficient B			2.66130e-01
Coefficient C			7.02250e+02
Coefficient D			2.87200e-01
Temperature range, min.			230.20
Temperature range, max.			702.25
ρl	941.47	kg/m3	230.20	Calculated Property
ρl	905.20	kg/m3	282.65	Calculated Property
ρl	867.14	kg/m3	335.10	Calculated Property
ρl	826.84	kg/m3	387.55	Calculated Property
ρl	783.67	kg/m3	440.00	Calculated Property
ρl	736.61	kg/m3	492.45	Calculated Property
ρl	683.93	kg/m3	544.90	Calculated Property
ρl	622.14	kg/m3	597.35	Calculated Property
ρl	541.72	kg/m3	649.80	Calculated Property
ρl	288.99	kg/m3	702.25	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 1.42e-05]	N/m	[230.20; 696.11]	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			-7.31020e-03
Coefficient B			1.59630e+02
Coefficient C			-4.11520e+00
Coefficient D			3.03690e-03
Coefficient E			-6.48960e-06
Comment			Range stopped where the equation turns negative; ChemSep gives it to 702.25 K.
Temperature range, min.			230.20
Temperature range, max.			696.11
γ	0.04	N/m	230.20	Calculated Property
γ	0.03	N/m	281.97	Calculated Property
γ	0.03	N/m	333.74	Calculated Property
γ	0.02	N/m	385.50	Calculated Property
γ	0.02	N/m	437.27	Calculated Property
γ	0.01	N/m	489.04	Calculated Property
γ	0.01	N/m	540.81	Calculated Property
γ	0.01	N/m	592.58	Calculated Property
γ	0.00	N/m	644.35	Calculated Property
γ	1.42e-05	N/m	696.11	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.27]	W/m×K	[230.20; 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			1.75930e-06
Coefficient B			1.77420e+00
Coefficient C			3.17620e+02
Coefficient D			3.76050e+04
Temperature range, min.			230.20
Temperature range, max.			1000.00
λgas	0.01	W/m×K	230.20	Calculated Property
λgas	0.02	W/m×K	315.73	Calculated Property
λgas	0.04	W/m×K	401.27	Calculated Property
λgas	0.06	W/m×K	486.80	Calculated Property
λgas	0.08	W/m×K	572.33	Calculated Property
λgas	0.11	W/m×K	657.87	Calculated Property
λgas	0.15	W/m×K	743.40	Calculated Property
λgas	0.18	W/m×K	828.93	Calculated Property
λgas	0.23	W/m×K	914.47	Calculated Property
λgas	0.27	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.11; 0.10]	W/m×K	[293.15; 468.96]	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			8.75970e-02
Coefficient B			-1.01000e+02
Coefficient C			-1.02530e+00
Coefficient D			-9.01740e-03
Coefficient E			4.50640e-06
Temperature range, min.			293.15
Temperature range, max.			468.96
λliquid	0.11	W/m×K	293.15	Calculated Property
λliquid	0.11	W/m×K	312.68	Calculated Property
λliquid	0.11	W/m×K	332.22	Calculated Property
λliquid	0.11	W/m×K	351.75	Calculated Property
λliquid	0.11	W/m×K	371.29	Calculated Property
λliquid	0.10	W/m×K	390.82	Calculated Property
λliquid	0.10	W/m×K	410.36	Calculated Property
λliquid	0.10	W/m×K	429.89	Calculated Property
λliquid	0.10	W/m×K	449.43	Calculated Property
λliquid	0.10	W/m×K	468.96	Calculated Property

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

• 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 5 ChEDL chemicals 1.5.2, from Daubert, T. E. Vapor-Liquid Critical Properties of Elements and Compounds. 5. Branched Alkanes and Cycloalkanes. J. Chem. Eng. Data 1996, 41, 365-372.
• 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.
• Cheméo Relay (1.0)
• 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
• 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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