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

• 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).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : 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_boilr : Boiling point at reduced pressure (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	[-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
ΔfH°gas	[-182.20; -180.20]	kJ/mol
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	3025.61	kPa	Joback Calculated Property
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
I	[1156.00; 1227.00]
I	1160.90		NIST
I	1170.00		NIST
I	1209.00		NIST
I	1195.00		NIST
I	1218.00		NIST
I	1161.00		NIST
I	1227.00		NIST
I	1156.00		NIST
I	1163.00		NIST
I	1170.00		NIST
I	1160.90		NIST
S°liquid	264.93	J/mol×K	NIST
Tboil	[456.40; 462.90]	K
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	[687.00; 960.15]	K
Tc	687.00 ± 3.00	K	NIST
Tc	960.15 ± 1.30	K	NIST
Tfus	[237.00; 242.80]	K
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; 242.77]	K
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

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	[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
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	[2.13; 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
Pvap	[1.33; 202.64]	kPa	[334.57; 491.98]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
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

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

• Cheméo Relay (1.0)
• 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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