Chemical Properties of Naphthalene, decahydro-, trans- (CAS 493-02-7)

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-MGCOHNPYSA-N

Formula

C10H18

SMILES

C1CCC2CCCCC2C1

Molecular Weight¹

138.25

CAS

493-02-7

Other Names

• (E)-Decahydronaphthalene
• Decahydronaphthalene, (E)-
• Decahydronaphthalene, trans-
• t-Decalin
• trans-Decaline
• trans-bicyclo[4.4.0]decane
• trans-decahydronaphthalene
• trans-decalin
• trans-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).
• 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°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_boilr : Boiling point at reduced pressure (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	[0.2536; 0.2756]
ω	0.2756		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.2738		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.2536		ChemSep v8.3 pure component data Compiled value
ΔcH°liquid	[-6278.90; -6255.90]	kJ/mol
ΔcH°liquid	-6276.96 ± 0.92	kJ/mol	NIST
ΔcH°liquid	-6278.90 ± 1.30	kJ/mol	NIST
ΔcH°liquid	-6264.00 ± 2.00	kJ/mol	NIST
ΔcH°liquid	-6255.90	kJ/mol	NIST
ΔcH°liquid	-6268.20 ± 4.60	kJ/mol	NIST
μ	0.00	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	73.55	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	[-182.20; -180.20]	kJ/mol
ΔfH°gas	-182.17	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-182.20 ± 2.30	kJ/mol	NIST
ΔfH°gas	-180.20	kJ/mol	NIST
ΔfH°liquid	[-230.70; -228.70]	kJ/mol
ΔfH°liquid	-230.70 ± 0.92	kJ/mol	NIST
ΔfH°liquid	-228.70 ± 1.30	kJ/mol	NIST
ΔfusH°	9.53	kJ/mol	Joback Calculated Property
ΔsubH°	64.30	kJ/mol	NIST
ΔvapH°	[42.84; 48.50]	kJ/mol
ΔvapH°	48.50 ± 2.10	kJ/mol	NIST
ΔvapH°	48.50	kJ/mol	NIST
ΔvapH°	42.84	kJ/mol	NIST
IE	[9.32; 9.38]	eV
IE	9.32 ± 0.05	eV	NIST
IE	9.32 ± 0.05	eV	NIST
IE	9.38 ± 0.01	eV	NIST
IE	9.35	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	[2837.10; 3150.90]	kPa
Pc	3141.08	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	2837.10	kPa	ChemSep v8.3 pure component data Compiled value
Ptriple	1.15e-03	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[1037.52; 1097.00]
Inp	1059.00		NIST
Inp	1059.00		NIST
Inp	1068.00		NIST
Inp	1085.00		NIST
Inp	1057.00		NIST
Inp	1057.00		NIST
Inp	1062.00		NIST
Inp	1051.00		NIST
Inp	1041.70		NIST
Inp	1078.00		NIST
Inp	Outlier 1090.00		NIST
Inp	1049.00		NIST
Inp	1064.70		NIST
Inp	1069.30		NIST
Inp	1082.50		NIST
Inp	1064.70		NIST
Inp	1069.30		NIST
Inp	1064.00		NIST
Inp	1087.00		NIST
Inp	1070.00		NIST
Inp	1082.00		NIST
Inp	1081.00		NIST
Inp	1061.00		NIST
Inp	1043.00		NIST
Inp	Outlier 1097.00		NIST
Inp	1052.85		NIST
Inp	1055.00		NIST
Inp	1051.80		NIST
Inp	1049.80		NIST
Inp	1045.70		NIST
Inp	1051.80		NIST
Inp	1055.90		NIST
Inp	1038.70		NIST
Inp	1045.70		NIST
Inp	1051.80		NIST
Inp	1055.90		NIST
Inp	1051.80		NIST
Inp	1049.80		NIST
Inp	1048.00		NIST
Inp	1047.88		NIST
Inp	1037.52		NIST
Inp	1044.69		NIST
Inp	1049.50		NIST
Inp	1048.56		NIST
Inp	1056.17		NIST
Inp	1061.35		NIST
Inp	1043.00		NIST
Inp	1049.00		NIST
Inp	1075.00		NIST
Inp	1076.00		NIST
Inp	1080.00		NIST
Inp	1074.00		NIST
Inp	1084.00		NIST
Inp	1061.00		NIST
Inp	1075.00		NIST
Inp	1078.00		NIST
Inp	1057.00		NIST
Inp	1046.00		NIST
Inp	1051.00		NIST
Inp	1053.00		NIST
Inp	1066.00		NIST
Inp	1075.00		NIST
Inp	1058.00		NIST
Inp	1057.00		NIST
Inp	1057.00		NIST
Inp	1042.00		NIST
Inp	1049.00		NIST
Inp	1057.00		NIST
Inp	1075.00		NIST
Inp	1049.00		NIST
Ip	[1156.00; 1227.00]
Ip	1160.90		NIST
Ip	1170.00		NIST
Ip	1209.00		NIST
Ip	1195.00		NIST
Ip	1218.00		NIST
Ip	1161.00		NIST
Ip	1227.00		NIST
Ip	1156.00		NIST
Ip	1163.00		NIST
Ip	1170.00		NIST
Ip	1160.90		NIST
S°liquid	264.93	J/mol×K	NIST
Tboil	[456.40; 462.90]	K
Tboil	460.46	K	ChemSep v8.3 pure component data Compiled value
Tboil	460.40	K	NIST
Tboil	458.65 ± 0.50	K	NIST
Tboil	459.90 ± 2.00	K	NIST
Tboil	460.42 ± 1.00	K	NIST
Tboil	460.40 ± 0.30	K	NIST
Tboil	462.90 ± 2.00	K	NIST
Tboil	459.00 ± 1.00	K	NIST
Tboil	460.70 ± 2.00	K	NIST
Tboil	458.70 ± 2.00	K	NIST
Tboil	456.40 ± 3.00	K	NIST
Tboil	458.40 ± 3.00	K	NIST
Tboil	457.90 ± 4.00	K	NIST
Tboil	458.00 ± 4.00	K	NIST
Tboil	458.00 ± 4.00	K	NIST
Tboil	458.00 ± 4.00	K	NIST
Tboil	462.00 ± 4.00	K	NIST
Tboil	462.00 ± 4.00	K	NIST
Tc	[686.93; 960.15]	K
Tc	687.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value
Tc	690.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	686.93	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	687.05	K	ChemSep v8.3 pure component data Compiled value
Tc	687.00 ± 3.00	K	NIST
Tc	Outlier 960.15 ± 1.30	K	NIST
Tfus	[237.00; 242.80]	K
Tfus	242.77	K	ChemSep v8.3 pure component data Compiled value
Tfus	242.75 ± 0.50	K	NIST
Tfus	242.80 ± 0.50	K	NIST
Tfus	242.75 ± 0.05	K	NIST
Tfus	242.75 ± 0.04	K	NIST
Tfus	242.76 ± 0.02	K	NIST
Tfus	242.80 ± 0.30	K	NIST
Tfus	240.45 ± 1.00	K	NIST
Tfus	242.73 ± 0.06	K	NIST
Tfus	242.64 ± 0.04	K	NIST
Tfus	242.75 ± 0.02	K	NIST
Tfus	242.66 ± 0.40	K	NIST
Tfus	242.39 ± 0.30	K	NIST
Tfus	242.43 ± 0.50	K	NIST
Tfus	241.67 ± 0.50	K	NIST
Tfus	240.00 ± 5.00	K	NIST
Tfus	Outlier 237.00 ± 5.00	K	NIST
Ttriple	[242.40; 242.79]	K
Ttriple	242.79	K	ChemSep v8.3 pure component data Compiled value
Ttriple	242.77 ± 0.07	K	NIST
Ttriple	242.77 ± 0.05	K	NIST
Ttriple	242.40 ± 0.20	K	NIST
Ttriple	242.77 ± 0.07	K	NIST
Ttriple	242.77 ± 0.05	K	NIST
Ttriple	242.40 ± 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	0.2380000		ChemSep v8.3 pure component data Compiled value
Zra	0.27		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[237.53; 272.29]	J/mol×K	[400.00; 450.00]
Cp,gas	237.53	J/mol×K	400.00	NIST
Cp,gas	272.29	J/mol×K	450.00	NIST
Cp,liquid	[202.20; 306.60]	J/mol×K	[250.00; 410.00]
Cp,liquid	202.20	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	207.20	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	212.50	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	214.20	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	217.90	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	223.60	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	226.86	J/mol×K	298.00	NIST
Cp,liquid	228.30	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	229.17	J/mol×K	298.15	NIST
Cp,liquid	229.17	J/mol×K	298.15	NIST
Cp,liquid	228.49	J/mol×K	298.15	NIST
Cp,liquid	229.17	J/mol×K	298.15	NIST
Cp,liquid	217.72	J/mol×K	298.15	NIST
Cp,liquid	229.40	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	235.50	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	250.60	J/mol×K	313.00	NIST
Cp,liquid	241.70	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	248.10	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	254.70	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	261.60	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	268.60	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	275.80	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	283.20	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	290.80	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	298.60	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
ΔfusH	[2.13; 9.49]	kJ/mol	[216.10; 242.40]
ΔfusH	2.13	kJ/mol	216.10	NIST
ΔfusH	9.49	kJ/mol	230.20	NIST
ΔfusH	9.49	kJ/mol	230.20	NIST
ΔfusH	3.24	kJ/mol	242.40	NIST
ΔfusH	3.24	kJ/mol	242.40	NIST
ΔsubH	66.20	kJ/mol	241.00	NIST
ΔvapH	44.20	kJ/mol	412.00	NIST
n0	1.46820		298.20	Liquid liquid equilibrium data for water + ethanol + trans-decalin: Measurement and predication
ρl	[809.40; 869.78]	kg/m3	[293.15; 373.15]
ρl	869.75	kg/m3	293.15	Density and Viscosity from 293.15 to 373.15 K, Speed of Sound and Bulk Modulus from 293.15 to 343.15 K, Surface Tension, and Flash Point of Binary Mixtures of Bicyclohexyl and 1,2,3,4-Tetrahydronaphthalene or Trans-decahydronaphthalene at 0.1 MPa
ρl	869.78	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	866.07	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	862.34	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	862.29	kg/m3	303.15	Density and Viscosity from 293.15 to 373.15 K, Speed of Sound and Bulk Modulus from 293.15 to 343.15 K, Surface Tension, and Flash Point of Binary Mixtures of Bicyclohexyl and 1,2,3,4-Tetrahydronaphthalene or Trans-decahydronaphthalene at 0.1 MPa
ρl	858.61	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	854.82	kg/m3	313.15	Density and Viscosity from 293.15 to 373.15 K, Speed of Sound and Bulk Modulus from 293.15 to 343.15 K, Surface Tension, and Flash Point of Binary Mixtures of Bicyclohexyl and 1,2,3,4-Tetrahydronaphthalene or Trans-decahydronaphthalene at 0.1 MPa
ρl	854.88	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	851.14	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	847.34	kg/m3	323.15	Density and Viscosity from 293.15 to 373.15 K, Speed of Sound and Bulk Modulus from 293.15 to 343.15 K, Surface Tension, and Flash Point of Binary Mixtures of Bicyclohexyl and 1,2,3,4-Tetrahydronaphthalene or Trans-decahydronaphthalene at 0.1 MPa
ρl	847.40	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
ρl	839.83	kg/m3	333.15	Density and Viscosity from 293.15 to 373.15 K, Speed of Sound and Bulk Modulus from 293.15 to 343.15 K, Surface Tension, and Flash Point of Binary Mixtures of Bicyclohexyl and 1,2,3,4-Tetrahydronaphthalene or Trans-decahydronaphthalene at 0.1 MPa
ρl	832.30	kg/m3	343.15	Density and Viscosity from 293.15 to 373.15 K, Speed of Sound and Bulk Modulus from 293.15 to 343.15 K, Surface Tension, and Flash Point of Binary Mixtures of Bicyclohexyl and 1,2,3,4-Tetrahydronaphthalene or Trans-decahydronaphthalene at 0.1 MPa
ρl	824.70	kg/m3	353.15	Density and Viscosity from 293.15 to 373.15 K, Speed of Sound and Bulk Modulus from 293.15 to 343.15 K, Surface Tension, and Flash Point of Binary Mixtures of Bicyclohexyl and 1,2,3,4-Tetrahydronaphthalene or Trans-decahydronaphthalene at 0.1 MPa
ρl	817.00	kg/m3	363.15	Density and Viscosity from 293.15 to 373.15 K, Speed of Sound and Bulk Modulus from 293.15 to 343.15 K, Surface Tension, and Flash Point of Binary Mixtures of Bicyclohexyl and 1,2,3,4-Tetrahydronaphthalene or Trans-decahydronaphthalene at 0.1 MPa
ρl	809.40	kg/m3	373.15	Density and Viscosity from 293.15 to 373.15 K, Speed of Sound and Bulk Modulus from 293.15 to 343.15 K, Surface Tension, and Flash Point of Binary Mixtures of Bicyclohexyl and 1,2,3,4-Tetrahydronaphthalene or Trans-decahydronaphthalene at 0.1 MPa
ΔfusS	[9.87; 41.22]	J/mol×K	[216.10; 242.40]
ΔfusS	9.87	J/mol×K	216.10	NIST
ΔfusS	41.22	J/mol×K	230.20	NIST
ΔfusS	13.40	J/mol×K	242.40	NIST
ΔfusS	13.40	J/mol×K	242.40	NIST

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboilr	458.20	K	101.00	NIST

Datasets

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
303.15	100.00	862.1
303.15	5000.00	865.4
303.15	10000.00	868.7
303.15	15000.00	871.6
303.15	20000.00	874.6
303.15	25000.00	877.6
303.15	30000.00	880.3
303.15	35000.00	882.9
303.15	40000.00	885.6
303.15	45000.00	888.2
303.15	50000.00	890.6
303.15	55000.00	893.0
303.15	60000.00	895.3
303.15	65000.00	897.6
323.15	100.00	847.1
323.15	5000.00	850.9
323.15	10000.00	854.4
323.15	15000.00	857.8
323.15	20000.00	861.0
323.15	25000.00	864.1
323.15	30000.00	867.1
323.15	35000.00	870.0
323.15	40000.00	872.8
323.15	45000.00	875.6
323.15	50000.00	878.3
323.15	55000.00	880.8
323.15	60000.00	883.4
323.15	65000.00	885.8
343.15	100.00	832.0
343.15	5000.00	836.2
343.15	10000.00	840.1
343.15	15000.00	843.9
343.15	20000.00	847.4
343.15	25000.00	850.8
343.15	30000.00	854.1
343.15	35000.00	857.2
343.15	40000.00	860.3
343.15	45000.00	863.2
343.15	50000.00	866.1
343.15	55000.00	868.8
343.15	60000.00	871.5
343.15	65000.00	874.2
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[89.86; 562.10]	J/mol×K	[150.00; 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			8.13510e+01
Coefficient B			-7.07340e+02
Coefficient C			6.88524e+00
Coefficient D			-1.89440e-04
Coefficient E			2.03650e-08
Temperature range, min.			150.00
Temperature range, max.			1500.00
Cp,gas	89.86	J/mol×K	150.00	Calculated Property
Cp,gas	168.92	J/mol×K	300.00	Calculated Property
Cp,gas	268.57	J/mol×K	450.00	Calculated Property
Cp,gas	351.78	J/mol×K	600.00	Calculated Property
Cp,gas	415.47	J/mol×K	750.00	Calculated Property
Cp,gas	463.31	J/mol×K	900.00	Calculated Property
Cp,gas	499.20	J/mol×K	1050.00	Calculated Property
Cp,gas	526.23	J/mol×K	1200.00	Calculated Property
Cp,gas	546.64	J/mol×K	1350.00	Calculated Property
Cp,gas	562.10	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[197.66; 336.52]	J/mol×K	[242.79; 460.46]	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			1.10470e+02
Coefficient B			-8.16290e+01
Coefficient C			3.40524e+00
Coefficient D			6.87810e-03
Coefficient E			-4.59520e-06
Temperature range, min.			242.79
Temperature range, max.			460.46
Cp,liquid	197.66	J/mol×K	242.79	Calculated Property
Cp,liquid	210.78	J/mol×K	266.98	Calculated Property
Cp,liquid	224.67	J/mol×K	291.16	Calculated Property
Cp,liquid	239.29	J/mol×K	315.35	Calculated Property
Cp,liquid	254.56	J/mol×K	339.53	Calculated Property
Cp,liquid	270.38	J/mol×K	363.72	Calculated Property
Cp,liquid	286.63	J/mol×K	387.90	Calculated Property
Cp,liquid	303.18	J/mol×K	412.09	Calculated Property
Cp,liquid	319.87	J/mol×K	436.27	Calculated Property
Cp,liquid	336.52	J/mol×K	460.46	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0073163; 0.0001128]	Pa×s	[242.79; 687.05]	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			-4.72100e+01
Coefficient B			3.03790e+03
Coefficient C			5.46820e+00
Coefficient D			-4.28420e-06
Coefficient E			2.00000e+00
Temperature range, min.			242.79
Temperature range, max.			687.05
η	0.0073163	Pa×s	242.79	Calculated Property
η	0.0021704	Pa×s	292.15	Calculated Property
η	0.0009916	Pa×s	341.51	Calculated Property
η	0.0005779	Pa×s	390.88	Calculated Property
η	0.0003886	Pa×s	440.24	Calculated Property
η	0.0002846	Pa×s	489.60	Calculated Property
η	0.0002193	Pa×s	538.96	Calculated Property
η	0.0001739	Pa×s	588.33	Calculated Property
η	0.0001398	Pa×s	637.69	Calculated Property
η	0.0001128	Pa×s	687.05	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[52.90; 0.00]	kJ/mol	[242.79; 687.05]	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			7.64616e+01
Coefficient B			9.18445e-01
Coefficient C			3.95142e-01
Coefficient D			-2.20243e+00
Coefficient E			1.39835e+00
Critical temperature, Tc (K)			6.87050e+02
Temperature range, min.			242.79
Temperature range, max.			687.05
ΔvapH	52.90	kJ/mol	242.79	Calculated Property
ΔvapH	49.21	kJ/mol	292.15	Calculated Property
ΔvapH	45.90	kJ/mol	341.51	Calculated Property
ΔvapH	42.86	kJ/mol	390.88	Calculated Property
ΔvapH	39.90	kJ/mol	440.24	Calculated Property
ΔvapH	36.75	kJ/mol	489.60	Calculated Property
ΔvapH	32.97	kJ/mol	538.96	Calculated Property
ΔvapH	27.89	kJ/mol	588.33	Calculated Property
ΔvapH	20.18	kJ/mol	637.69	Calculated Property
ΔvapH	0.00	kJ/mol	687.05	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.64]	kPa	[334.57; 491.98]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.37820e+01
Coefficient B			-3.58156e+03
Coefficient C			-6.91580e+01
Temperature range, min.			334.57
Temperature range, max.			491.98
Pvap	1.33	kPa	334.57	Calculated Property
Pvap	3.07	kPa	352.06	Calculated Property
Pvap	6.42	kPa	369.55	Calculated Property
Pvap	12.37	kPa	387.04	Calculated Property
Pvap	22.26	kPa	404.53	Calculated Property
Pvap	37.79	kPa	422.02	Calculated Property
Pvap	61.03	kPa	439.51	Calculated Property
Pvap	94.39	kPa	457.00	Calculated Property
Pvap	140.60	kPa	474.49	Calculated Property
Pvap	202.64	kPa	491.98	Calculated Property
Pvap	[1.22e-03; 2837.10]	kPa	[242.79; 678.44]	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			1.05098e+02
Coefficient B			-9.61931e+03
Coefficient C			-1.32181e+01
Coefficient D			6.97444e-06
Coefficient E			2.00000e+00
Comment			Range stopped where the equation exceeds Pc; ChemSep gives it to 687.05 K.
Temperature range, min.			242.79
Temperature range, max.			678.44
Pvap	1.22e-03	kPa	242.79	Calculated Property
Pvap	0.10	kPa	291.20	Calculated Property
Pvap	1.72	kPa	339.60	Calculated Property
Pvap	12.98	kPa	388.01	Calculated Property
Pvap	56.68	kPa	436.41	Calculated Property
Pvap	173.94	kPa	484.82	Calculated Property
Pvap	422.27	kPa	533.22	Calculated Property
Pvap	875.54	kPa	581.63	Calculated Property
Pvap	1632.52	kPa	630.03	Calculated Property
Pvap	2837.10	kPa	678.44	Calculated Property
Pvap	[5.53; 102.74]	kPa	[365.51; 461.02]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.37995e+01
Coefficient B			-3.62173e+03
Coefficient C			-6.59470e+01
Reference			Camin and Rossini, 1955
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			365.51
Temperature range, max.			461.02
Pvap	5.53	kPa	365.51	Calculated Property
Pvap	8.36	kPa	376.12	Calculated Property
Pvap	12.30	kPa	386.73	Calculated Property
Pvap	17.65	kPa	397.35	Calculated Property
Pvap	24.78	kPa	407.96	Calculated Property
Pvap	34.08	kPa	418.57	Calculated Property
Pvap	46.00	kPa	429.18	Calculated Property
Pvap	61.06	kPa	439.80	Calculated Property
Pvap	79.77	kPa	450.41	Calculated Property
Pvap	102.74	kPa	461.02	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[907.08; 286.78]	kg/m3	[242.79; 687.05]	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			7.74061e+01
Coefficient B			2.69910e-01
Coefficient C			6.87050e+02
Coefficient D			2.95200e-01
Temperature range, min.			242.79
Temperature range, max.			687.05
ρl	907.08	kg/m3	242.79	Calculated Property
ρl	872.08	kg/m3	292.15	Calculated Property
ρl	835.39	kg/m3	341.51	Calculated Property
ρl	796.59	kg/m3	390.88	Calculated Property
ρl	755.07	kg/m3	440.24	Calculated Property
ρl	709.88	kg/m3	489.60	Calculated Property
ρl	659.38	kg/m3	538.96	Calculated Property
ρl	600.27	kg/m3	588.33	Calculated Property
ρl	523.58	kg/m3	637.69	Calculated Property
ρl	286.78	kg/m3	687.05	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 1.93e-05]	N/m	[242.79; 680.83]	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			-7.29920e-03
Coefficient B			1.37990e+02
Coefficient C			-3.96960e+00
Coefficient D			2.50430e-03
Coefficient E			-6.16020e-06
Comment			Range stopped where the equation turns negative; ChemSep gives it to 687.05 K.
Temperature range, min.			242.79
Temperature range, max.			680.83
γ	0.04	N/m	242.79	Calculated Property
γ	0.03	N/m	291.46	Calculated Property
γ	0.03	N/m	340.13	Calculated Property
γ	0.02	N/m	388.80	Calculated Property
γ	0.02	N/m	437.47	Calculated Property
γ	0.01	N/m	486.15	Calculated Property
γ	0.01	N/m	534.82	Calculated Property
γ	0.01	N/m	583.49	Calculated Property
γ	0.00	N/m	632.16	Calculated Property
γ	1.93e-05	N/m	680.83	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.26]	W/m×K	[242.79; 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			-1.39280e+01
Coefficient B			6.54480e-01
Coefficient C			-2.83730e+06
Coefficient D			-2.04300e+09
Temperature range, min.			242.79
Temperature range, max.			1000.00
λgas	0.01	W/m×K	242.79	Calculated Property
λgas	0.02	W/m×K	326.92	Calculated Property
λgas	0.04	W/m×K	411.06	Calculated Property
λgas	0.06	W/m×K	495.19	Calculated Property
λgas	0.08	W/m×K	579.33	Calculated Property
λgas	0.11	W/m×K	663.46	Calculated Property
λgas	0.14	W/m×K	747.60	Calculated Property
λgas	0.18	W/m×K	831.73	Calculated Property
λgas	0.22	W/m×K	915.87	Calculated Property
λgas	0.26	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.11; 0.10]	W/m×K	[293.15; 460.46]	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			8.77710e-02
Coefficient B			4.54150e+01
Coefficient C			-2.16130e+00
Coefficient D			-6.19390e-03
Coefficient E			2.21590e-06
Temperature range, min.			293.15
Temperature range, max.			460.46
λliquid	0.11	W/m×K	293.15	Calculated Property
λliquid	0.11	W/m×K	311.74	Calculated Property
λliquid	0.11	W/m×K	330.33	Calculated Property
λliquid	0.11	W/m×K	348.92	Calculated Property
λliquid	0.11	W/m×K	367.51	Calculated Property
λliquid	0.10	W/m×K	386.10	Calculated Property
λliquid	0.10	W/m×K	404.69	Calculated Property
λliquid	0.10	W/m×K	423.28	Calculated Property
λliquid	0.10	W/m×K	441.87	Calculated Property
λliquid	0.10	W/m×K	460.46	Calculated Property

Similar Compounds

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

Mixtures

• Naphthalene, decahydro-, cis- + Naphthalene, decahydro-, trans- + Dibenzothiophene
• Naphthalene, decahydro-, cis- + Naphthalene, decahydro-, trans-
• Naphthalene, decahydro-, cis- + Naphthalene, decahydro-, trans- + Decane
• Naphthalene, decahydro-, cis- + Hexadecane + Naphthalene, decahydro-, trans-
• Ethanol + Naphthalene, decahydro-, trans- + Water
• Naphthalene, decahydro-, cis- + Naphthalene, 1,2,3,4-tetrahydro- + Naphthalene, decahydro-, trans-
• Naphthalene, decahydro-, trans- + 1,1'-Bicyclohexyl
• Naphthalene, decahydro-, cis- + Naphthalene, decahydro-, trans- + Cyclohexane
• Toluene + Naphthalene, decahydro-, cis- + Naphthalene, decahydro-, trans-
• Naphthalene, decahydro-, trans- + Nonane
• Naphthalene, decahydro-, trans- + Decane
• Undecane + Naphthalene, decahydro-, trans-
• Naphthalene, 1,2,3,4-tetrahydro- + Naphthalene, decahydro-, trans-
• 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

• 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
• Liquid liquid equilibrium data for water + ethanol + trans-decalin: Measurement and predication
• 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 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
• Density and Viscosity from 293.15 to 373.15 K, Speed of Sound and Bulk Modulus from 293.15 to 343.15 K, Surface Tension, and Flash Point of Binary Mixtures of Bicyclohexyl and 1,2,3,4-Tetrahydronaphthalene or Trans-decahydronaphthalene at 0.1 MPa
• Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of 1,2,3,4-Tetrahydronaphthalene and Trans-decahydronaphthalene
• 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
• 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
• 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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