Naphthalene, decahydro-, trans- (CAS 493-02-7)

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Physical Properties

Property	Value	Unit	Source
Δ_cH°_liquid	[-6278.90; -6255.90]	kJ/mol
Δ_cH°_liquid	-6276.96 ± 0.92	kJ/mol	NIST
Δ_cH°_liquid	-6278.90 ± 1.30	kJ/mol	NIST
Δ_cH°_liquid	-6264.00 ± 2.00	kJ/mol	NIST
Δ_cH°_liquid	-6255.90	kJ/mol	NIST
Δ_cH°_liquid	-6268.20 ± 4.60	kJ/mol	NIST
Δ_fG°	106.42	kJ/mol	Joback Calculated Property
Δ_fH°_gas	[-182.20; -180.20]	kJ/mol
Δ_fH°_gas	-182.20 ± 2.30	kJ/mol	NIST
Δ_fH°_gas	-180.20	kJ/mol	NIST
Δ_fH°_liquid	[-230.70; -228.70]	kJ/mol
Δ_fH°_liquid	-230.70 ± 0.92	kJ/mol	NIST
Δ_fH°_liquid	-228.70 ± 1.30	kJ/mol	NIST
Δ_fusH°	9.53	kJ/mol	Joback Calculated Property
Δ_subH°	64.30	kJ/mol	NIST
Δ_vapH°	[42.84; 48.50]	kJ/mol
Δ_vapH°	48.50 ± 2.10	kJ/mol	NIST
Δ_vapH°	48.50	kJ/mol	NIST
Δ_vapH°	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	-3.31		Crippen Calculated Property
logP_oct/wat	3.367		Crippen Calculated Property
McVol	130.040	ml/mol	McGowan Calculated Property
P_c	3025.61	kPa	Joback Calculated Property
I_np	[1037.52; 1097.00]
I_np	1059.00		NIST
I_np	1059.00		NIST
I_np	1068.00		NIST
I_np	1085.00		NIST
I_np	1057.00		NIST
I_np	1057.00		NIST
I_np	1062.00		NIST
I_np	1051.00		NIST
I_np	1041.70		NIST
I_np	1078.00		NIST
I_np	Outlier 1090.00		NIST
I_np	1049.00		NIST
I_np	1064.70		NIST
I_np	1069.30		NIST
I_np	1082.50		NIST
I_np	1064.70		NIST
I_np	1069.30		NIST
I_np	1064.00		NIST
I_np	1087.00		NIST
I_np	1070.00		NIST
I_np	1082.00		NIST
I_np	1081.00		NIST
I_np	1061.00		NIST
I_np	1043.00		NIST
I_np	Outlier 1097.00		NIST
I_np	1052.85		NIST
I_np	1055.00		NIST
I_np	1051.80		NIST
I_np	1049.80		NIST
I_np	1045.70		NIST
I_np	1051.80		NIST
I_np	1055.90		NIST
I_np	1038.70		NIST
I_np	1045.70		NIST
I_np	1051.80		NIST
I_np	1055.90		NIST
I_np	1051.80		NIST
I_np	1049.80		NIST
I_np	1048.00		NIST
I_np	1047.88		NIST
I_np	1037.52		NIST
I_np	1044.69		NIST
I_np	1049.50		NIST
I_np	1048.56		NIST
I_np	1056.17		NIST
I_np	1061.35		NIST
I_np	1043.00		NIST
I_np	1049.00		NIST
I_np	1075.00		NIST
I_np	1076.00		NIST
I_np	1080.00		NIST
I_np	1074.00		NIST
I_np	1084.00		NIST
I_np	1061.00		NIST
I_np	1075.00		NIST
I_np	1078.00		NIST
I_np	1057.00		NIST
I_np	1046.00		NIST
I_np	1051.00		NIST
I_np	1053.00		NIST
I_np	1066.00		NIST
I_np	1075.00		NIST
I_np	1058.00		NIST
I_np	1057.00		NIST
I_np	1057.00		NIST
I_np	1042.00		NIST
I_np	1049.00		NIST
I_np	1057.00		NIST
I_np	1075.00		NIST
I_np	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
T_boil	458.76	K	Joback Calculated Property
T_c	[687.00; 960.15]	K
T_c	687.00 ± 3.00	K	NIST
T_c	960.15 ± 1.30	K	NIST
T_fus	224.26	K	Joback Calculated Property
T_triple	[242.40; 242.77]	K
T_triple	242.77 ± 0.07	K	NIST
T_triple	242.77 ± 0.05	K	NIST
T_triple	242.40 ± 0.20	K	NIST
V_c	0.477	m³/kmol	Joback Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
C_p,gas	[237.53; 272.29]	J/mol×K	[400.00; 450.00]
C_p,gas	237.53	J/mol×K	400.00	NIST
C_p,gas	272.29	J/mol×K	450.00	NIST
C_p,liquid	[217.72; 250.60]	J/mol×K	[298.00; 313.00]

C_p,liquid	226.86	J/mol×K	298.00	NIST
C_p,liquid	229.17	J/mol×K	298.15	NIST
C_p,liquid	229.17	J/mol×K	298.15	NIST
C_p,liquid	229.17	J/mol×K	298.15	NIST
C_p,liquid	228.49	J/mol×K	298.15	NIST
C_p,liquid	217.72	J/mol×K	298.15	NIST
C_p,liquid	250.60	J/mol×K	313.00	NIST
η	[0.0004040; 0.0046703]	Pa×s	[224.26; 458.76]

η	0.0046703	Pa×s	224.26	Joback Calculated Property
η	0.0022946	Pa×s	263.34	Joback Calculated Property
η	0.0013547	Pa×s	302.43	Joback Calculated Property
η	0.0009023	Pa×s	341.51	Joback Calculated Property
η	0.0006533	Pa×s	380.59	Joback Calculated Property
η	0.0005024	Pa×s	419.68	Joback Calculated Property
η	0.0004040	Pa×s	458.76	Joback Calculated Property
Δ_fusH	[2.13; 9.49]	kJ/mol	[216.10; 242.40]
Δ_fusH	2.13	kJ/mol	216.10	NIST
Δ_fusH	9.49	kJ/mol	230.20	NIST
Δ_fusH	9.49	kJ/mol	230.20	NIST
Δ_fusH	3.24	kJ/mol	242.40	NIST
Δ_subH	66.20	kJ/mol	241.00	NIST
Δ_vapH	44.20	kJ/mol	412.00	NIST
n₀	1.46820		298.20	Liquid ...
ρ_l	[809.40; 869.78]	kg/m³	[293.15; 373.15]

ρ_l	869.75	kg/m³	293.15	Density...
ρ_l	869.78	kg/m³	293.15	Excess ...
ρ_l	866.07	kg/m³	298.15	Excess ...
ρ_l	862.29	kg/m³	303.15	Density...
ρ_l	862.34	kg/m³	303.15	Excess ...
ρ_l	858.61	kg/m³	308.15	Excess ...
ρ_l	854.88	kg/m³	313.15	Excess ...
ρ_l	854.82	kg/m³	313.15	Density...
ρ_l	851.14	kg/m³	318.15	Excess ...
ρ_l	847.34	kg/m³	323.15	Density...
ρ_l	847.40	kg/m³	323.15	Excess ...
ρ_l	839.83	kg/m³	333.15	Density...
ρ_l	832.30	kg/m³	343.15	Density...
ρ_l	824.70	kg/m³	353.15	Density...
ρ_l	817.00	kg/m³	363.15	Density...
ρ_l	809.40	kg/m³	373.15	Density...
Δ_fusS	[9.87; 41.22]	J/mol×K	[216.10; 242.40]
Δ_fusS	9.87	J/mol×K	216.10	NIST
Δ_fusS	41.22	J/mol×K	230.20	NIST
Δ_fusS	13.40	J/mol×K	242.40	NIST

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
T_boilr	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
P_vap	[1.33; 202.64]	kPa	[334.57; 491.98]	The Yaw...
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

P_vap	1.33	kPa	334.57	Calculated Property
P_vap	3.07	kPa	352.06	Calculated Property
P_vap	6.42	kPa	369.55	Calculated Property
P_vap	12.37	kPa	387.04	Calculated Property
P_vap	22.26	kPa	404.53	Calculated Property
P_vap	37.79	kPa	422.02	Calculated Property
P_vap	61.03	kPa	439.51	Calculated Property
P_vap	94.39	kPa	457.00	Calculated Property
P_vap	140.60	kPa	474.49	Calculated Property
P_vap	202.64	kPa	491.98	Calculated Property

Similar Compounds

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

Mixtures

Sources

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

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