Naphthalene, 1,2,3,4-tetrahydro- (CAS 119-64-2)

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Physical Properties

Property	Value	Unit	Source
ω	0.3030		KDB
PAff	[800.80; 809.70]	kJ/mol
PAff	809.70	kJ/mol	NIST
PAff	800.80	kJ/mol	NIST
BasG	[774.00; 782.10]	kJ/mol
BasG	782.10	kJ/mol	NIST
BasG	774.00	kJ/mol	NIST
Δ_cH°_liquid	[-5621.54; -5581.90]	kJ/mol
Δ_cH°_liquid	-5621.54 ± 0.88	kJ/mol	NIST
Δ_cH°_liquid	-5617.50 ± 2.10	kJ/mol	NIST
Δ_cH°_liquid	-5598.60	kJ/mol	NIST
Δ_cH°_liquid	-5581.90	kJ/mol	NIST
Δ_fG°	167.10	kJ/mol	KDB
Δ_fH°_gas	[2.76; 30.00]	kJ/mol
Δ_fH°_gas	2.76	kJ/mol	KDB
Δ_fH°_gas	30.00	kJ/mol	NIST
Δ_fH°_gas	26.00 ± 2.00	kJ/mol	NIST
Δ_fH°_liquid	[-32.60; -28.60]	kJ/mol
Δ_fH°_liquid	-28.60 ± 1.00	kJ/mol	NIST
Δ_fH°_liquid	-32.60 ± 2.20	kJ/mol	NIST
Δ_fusH°	10.27	kJ/mol	Joback Calculated Property
Δ_vapH°	[55.00; 58.60]	kJ/mol
Δ_vapH°	55.00 ± 1.00	kJ/mol	NIST
Δ_vapH°	58.60	kJ/mol	NIST
IE	[8.44; 9.14]	eV
IE	8.46 ± 0.02	eV	NIST
IE	8.44	eV	NIST
IE	8.48 ± 0.05	eV	NIST
IE	8.47	eV	NIST
IE	8.73	eV	NIST
IE	Outlier 9.14 ± 0.05	eV	NIST
IE	8.45 ± 0.02	eV	NIST
IE	8.44	eV	NIST
log₁₀WS	-4.37		Aq. Solubility Prediction
logP_oct/wat	2.565		Crippen Calculated Property
McVol	117.140	ml/mol	McGowan Calculated Property
NFPA Fire	2		KDB
NFPA Health	1		KDB
P_c	[3630.00; 3750.00]	kPa
P_c	3650.00	kPa	KDB
P_c	3700.00 ± 100.00	kPa	NIST
P_c	3630.00 ± 25.00	kPa	NIST
P_c	3750.00 ± 80.00	kPa	NIST
ρ_c	[300.10; 330.51]	kg/m³
ρ_c	330.51 ± 13.22	kg/m³	NIST
ρ_c	323.90 ± 6.61	kg/m³	NIST
ρ_c	300.10 ± 14.54	kg/m³	NIST
I_np	[195.21; 1180.00]
I_np	1143.00		NIST
I_np	1143.00		NIST
I_np	1168.50		NIST
I_np	1142.80		NIST
I_np	1154.00		NIST
I_np	1180.00		NIST
I_np	1179.00		NIST
I_np	1170.00		NIST
I_np	1142.00		NIST
I_np	1142.00		NIST
I_np	1147.00		NIST
I_np	1136.00		NIST
I_np	1129.80		NIST
I_np	1164.00		NIST
I_np	1178.00		NIST
I_np	1137.00		NIST
I_np	1133.20		NIST
I_np	1137.60		NIST
I_np	1168.70		NIST
I_np	1179.80		NIST
I_np	1140.00		NIST
I_np	1142.00		NIST
I_np	1150.00		NIST
I_np	1155.00		NIST
I_np	1133.00		NIST
I_np	1137.00		NIST
I_np	1133.20		NIST
I_np	1137.60		NIST
I_np	1165.00		NIST
I_np	1168.00		NIST
I_np	1173.00		NIST
I_np	1140.00		NIST
I_np	1125.60		NIST
I_np	1150.00		NIST
I_np	1136.00		NIST
I_np	1163.35		NIST
I_np	1153.90		NIST
I_np	1151.70		NIST
I_np	1158.50		NIST
I_np	1162.50		NIST
I_np	1179.40		NIST
I_np	1142.90		NIST
I_np	1151.70		NIST
I_np	1158.50		NIST
I_np	1162.50		NIST
I_np	1140.47		NIST
I_np	1140.85		NIST
I_np	1141.00		NIST
I_np	1163.00		NIST
I_np	1130.46		NIST
I_np	1138.09		NIST
I_np	1142.95		NIST
I_np	1157.79		NIST
I_np	1166.27		NIST
I_np	1171.51		NIST
I_np	1136.00		NIST
I_np	1169.00		NIST
I_np	1133.00		NIST
I_np	1137.00		NIST
I_np	1142.00		NIST
I_np	1155.00		NIST
I_np	1147.00		NIST
I_np	1166.00		NIST
I_np	1169.00		NIST
I_np	1155.00		NIST
I_np	1148.00		NIST
I_np	1152.00		NIST
I_np	1162.00		NIST
I_np	1164.00		NIST
I_np	1174.00		NIST
I_np	1136.00		NIST
I_np	1147.00		NIST
I_np	1167.00		NIST
I_np	1137.00		NIST
I_np	1158.00		NIST
I_np	1171.00		NIST
I_np	1179.00		NIST
I_np	1137.00		NIST
I_np	1162.00		NIST
I_np	1163.00		NIST
I_np	1130.00		NIST
I_np	1144.00		NIST
I_np	1169.00		NIST
I_np	1142.10		NIST
I_np	1152.90		NIST
I_np	1149.70		NIST
I_np	1152.40		NIST
I_np	1141.00		NIST
I_np	1136.00		NIST
I_np	1153.00		NIST
I_np	Outlier 195.21		NIST
I_np	Outlier 195.47		NIST
I_np	Outlier 197.04		NIST
I_np	1133.00		NIST
I_np	1166.00		NIST
I_np	Outlier 195.21		NIST
I_np	1169.00		NIST
I_np	1164.00		NIST
I_np	1137.00		NIST
I	[1476.00; 1565.00]
I	1490.40		NIST
I	1476.00		NIST
I	1523.00		NIST
I	1517.00		NIST
I	1565.00		NIST
I	1565.00		NIST
I	1490.00		NIST
I	1525.00		NIST
I	1525.00		NIST
I	1525.00		NIST
I	1523.00		NIST
S°_liquid	251.46	J/mol×K	NIST
T_boil	[478.80; 484.15]	K
T_boil	481.45	K	Excess volumes, densities, speeds of sound and viscosities for the binary systems of diisopropyl ether with hydrocarbons at 303.15K
T_boil	480.77	K	KDB
T_boil	480.80	K	NIST
T_boil	Outlier 484.15 ± 5.00	K	NIST
T_boil	480.45 ± 0.50	K	NIST
T_boil	480.15 ± 0.50	K	NIST
T_boil	480.56 ± 0.10	K	NIST
T_boil	479.70 ± 1.00	K	NIST
T_boil	478.80 ± 0.50	K	NIST
T_c	[719.90; 721.70]	K
T_c	720.00	K	KDB
T_c	720.00 ± 1.00	K	NIST
T_c	721.70 ± 0.50	K	NIST
T_c	719.90 ± 1.00	K	NIST
T_c	721.00 ± 1.50	K	NIST
T_fus	[236.45; 242.55]	K
T_fus	237.40	K	KDB
T_fus	238.73	K	Aq. Solubility Prediction
T_fus	Outlier 242.55	K	NIST
T_fus	237.17 ± 0.20	K	NIST
T_fus	237.31 ± 0.06	K	NIST
T_fus	237.33 ± 0.04	K	NIST
T_fus	237.36 ± 0.03	K	NIST
T_fus	237.33 ± 0.20	K	NIST
T_fus	236.45 ± 0.50	K	NIST
T_fus	238.20 ± 0.60	K	NIST
T_triple	[237.34; 237.35]	K
T_triple	237.34 ± 0.07	K	NIST
T_triple	237.35 ± 0.05	K	NIST
T_triple	237.34 ± 0.07	K	NIST
T_triple	237.35 ± 0.05	K	NIST
V_c	[0.408; 0.408]	m³/kmol
V_c	0.408	m³/kmol	KDB
V_c	0.408	m³/kmol	NIST
Z_c	0.2487620		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
C_p,gas	[241.23; 324.45]	J/mol×K	[475.54; 708.10]

C_p,gas	241.23	J/mol×K	475.54	Joback Calculated Property
C_p,gas	257.83	J/mol×K	514.30	Joback Calculated Property
C_p,gas	273.25	J/mol×K	553.06	Joback Calculated Property
C_p,gas	287.54	J/mol×K	591.82	Joback Calculated Property
C_p,gas	300.80	J/mol×K	630.58	Joback Calculated Property
C_p,gas	313.07	J/mol×K	669.34	Joback Calculated Property
C_p,gas	324.45	J/mol×K	708.10	Joback Calculated Property
C_p,liquid	217.44	J/mol×K	298.15	NIST
C_sat	[195.70; 227.90]	J/mol×K	[250.00; 320.00]

C_sat	195.70	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
C_sat	200.00	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
C_sat	204.40	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
C_sat	205.80	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
C_sat	209.00	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
C_sat	213.60	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
C_sat	217.50	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
C_sat	218.30	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
C_sat	223.10	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
C_sat	227.90	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
η	[0.0003310; 0.0025839]	Pa×s	[260.06; 475.54]

η	0.0025839	Pa×s	260.06	Joback Calculated Property
η	0.0014903	Pa×s	295.97	Joback Calculated Property
η	0.0009683	Pa×s	331.89	Joback Calculated Property
η	0.0006844	Pa×s	367.80	Joback Calculated Property
η	0.0005146	Pa×s	403.71	Joback Calculated Property
η	0.0004053	Pa×s	439.63	Joback Calculated Property
η	0.0003310	Pa×s	475.54	Joback Calculated Property
Δ_fusH	[12.45; 12.45]	kJ/mol	[237.36; 237.40]
Δ_fusH	12.45	kJ/mol	237.36	NIST
Δ_fusH	12.45	kJ/mol	237.36	NIST
Δ_fusH	12.45	kJ/mol	237.40	NIST
Δ_fusH	12.45	kJ/mol	237.40	NIST
Δ_vapH	[32.00; 52.10]	kJ/mol	[384.00; 604.00]

Δ_vapH	52.10	kJ/mol	384.00	NIST
Δ_vapH	51.10	kJ/mol	396.00	NIST
Δ_vapH	48.60	kJ/mol	423.00	NIST
Δ_vapH	41.30 ± 0.10	kJ/mol	498.00	NIST
Δ_vapH	44.10	kJ/mol	522.50	NIST
Δ_vapH	37.60 ± 0.10	kJ/mol	552.00	NIST
Δ_vapH	35.70 ± 0.10	kJ/mol	567.00	NIST
Δ_vapH	33.90 ± 0.10	kJ/mol	585.00	NIST
Δ_vapH	32.00 ± 0.10	kJ/mol	604.00	NIST
n₀	[1.51790; 1.54155]		[293.15; 343.15]

n₀	1.54150		293.15	Densities, Sound Velocities, and Refractive Indexes of Tetralin + n-Hexadecane at (293.15, 303.15, 313.15, 323.15, 333.15, and 343.15) K
n₀	1.54155		293.15	Thermodynamic modeling and experimental speeds of sound, densities, and refractive indexes of (tetralin + n-dodecane)
n₀	1.54140		293.15	Densities, sound velocities, and refractive indexes of (tetralin + n-decane) and thermodynamic modeling by Prigogine-Flory-Patterson model
n₀	1.54000		293.15	Densities, Viscosities, and Refractive Indices of Binary Mixtures of 1,2,3,4-Tetrahydronaphthalene with Some n-Alkanes at T = (293.15 to 313.15) K
n₀	1.53919		298.15	KDB
n₀	1.53670		303.15	Densities, sound velocities, and refractive indexes of (tetralin + n-decane) and thermodynamic modeling by Prigogine-Flory-Patterson model
n₀	1.53600		303.15	Densities, Viscosities, and Refractive Indices of Binary Mixtures of 1,2,3,4-Tetrahydronaphthalene with Some n-Alkanes at T = (293.15 to 313.15) K
n₀	1.53687		303.15	Thermodynamic modeling and experimental speeds of sound, densities, and refractive indexes of (tetralin + n-dodecane)
n₀	1.53690		303.15	Densities, Sound Velocities, and Refractive Indexes of Tetralin + n-Hexadecane at (293.15, 303.15, 313.15, 323.15, 333.15, and 343.15) K
n₀	1.53210		313.15	Densities, sound velocities, and refractive indexes of (tetralin + n-decane) and thermodynamic modeling by Prigogine-Flory-Patterson model
n₀	1.53220		313.15	Densities, Sound Velocities, and Refractive Indexes of Tetralin + n-Hexadecane at (293.15, 303.15, 313.15, 323.15, 333.15, and 343.15) K
n₀	1.53216		313.15	Thermodynamic modeling and experimental speeds of sound, densities, and refractive indexes of (tetralin + n-dodecane)
n₀	1.52740		323.15	Densities, sound velocities, and refractive indexes of (tetralin + n-decane) and thermodynamic modeling by Prigogine-Flory-Patterson model
n₀	1.52752		323.15	Thermodynamic modeling and experimental speeds of sound, densities, and refractive indexes of (tetralin + n-dodecane)
n₀	1.52750		323.15	Densities, Sound Velocities, and Refractive Indexes of Tetralin + n-Hexadecane at (293.15, 303.15, 313.15, 323.15, 333.15, and 343.15) K
n₀	1.52274		333.15	Thermodynamic modeling and experimental speeds of sound, densities, and refractive indexes of (tetralin + n-dodecane)
n₀	1.52270		333.15	Densities, Sound Velocities, and Refractive Indexes of Tetralin + n-Hexadecane at (293.15, 303.15, 313.15, 323.15, 333.15, and 343.15) K
n₀	1.52280		333.15	Densities, sound velocities, and refractive indexes of (tetralin + n-decane) and thermodynamic modeling by Prigogine-Flory-Patterson model
n₀	1.51790		343.15	Densities, Sound Velocities, and Refractive Indexes of Tetralin + n-Hexadecane at (293.15, 303.15, 313.15, 323.15, 333.15, and 343.15) K
n₀	1.51795		343.15	Thermodynamic modeling and experimental speeds of sound, densities, and refractive indexes of (tetralin + n-dodecane)
n₀	1.51800		343.15	Densities, sound velocities, and refractive indexes of (tetralin + n-decane) and thermodynamic modeling by Prigogine-Flory-Patterson model
ρ_l	[904.80; 973.00]	kg/m³	[293.00; 373.15]

ρ_l	973.00	kg/m³	293.00	KDB
ρ_l	968.89	kg/m³	293.15	Densities and Viscosities for the Ternary System of 1,2,3,4-Tetrahydronaphthalene + Isopropylcyclohexane + Cyclopropanemethanol and Corresponding Binaries at T = (293.15 to 343.15) K
ρ_l	968.80	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
ρ_l	964.92	kg/m³	298.15	Densities and Viscosities for the Ternary System of 1,2,3,4-Tetrahydronaphthalene + Isopropylcyclohexane + Cyclopropanemethanol and Corresponding Binaries at T = (293.15 to 343.15) K
ρ_l	960.90	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
ρ_l	960.96	kg/m³	303.15	Densities and Viscosities for the Ternary System of 1,2,3,4-Tetrahydronaphthalene + Isopropylcyclohexane + Cyclopropanemethanol and Corresponding Binaries at T = (293.15 to 343.15) K
ρ_l	956.99	kg/m³	308.15	Densities and Viscosities for the Ternary System of 1,2,3,4-Tetrahydronaphthalene + Isopropylcyclohexane + Cyclopropanemethanol and Corresponding Binaries at T = (293.15 to 343.15) K
ρ_l	953.00	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
ρ_l	952.93	kg/m³	313.15	Experimental high pressure speed of sound and density of (tetralin + n-decane) and (tetralin + n-hexadecane) systems and thermodynamic modeling
ρ_l	953.03	kg/m³	313.15	Densities and Viscosities for the Ternary System of 1,2,3,4-Tetrahydronaphthalene + Isopropylcyclohexane + Cyclopropanemethanol and Corresponding Binaries at T = (293.15 to 343.15) K
ρ_l	949.05	kg/m³	318.15	Densities and Viscosities for the Ternary System of 1,2,3,4-Tetrahydronaphthalene + Isopropylcyclohexane + Cyclopropanemethanol and Corresponding Binaries at T = (293.15 to 343.15) K
ρ_l	945.00	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
ρ_l	945.10	kg/m³	323.15	Densities and Viscosities for the Ternary System of 1,2,3,4-Tetrahydronaphthalene + Isopropylcyclohexane + Cyclopropanemethanol and Corresponding Binaries at T = (293.15 to 343.15) K
ρ_l	944.99	kg/m³	323.15	Experimental high pressure speed of sound and density of (tetralin + n-decane) and (tetralin + n-hexadecane) systems and thermodynamic modeling
ρ_l	941.13	kg/m³	328.15	Densities and Viscosities for the Ternary System of 1,2,3,4-Tetrahydronaphthalene + Isopropylcyclohexane + Cyclopropanemethanol and Corresponding Binaries at T = (293.15 to 343.15) K
ρ_l	937.10	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
ρ_l	937.04	kg/m³	333.15	Experimental high pressure speed of sound and density of (tetralin + n-decane) and (tetralin + n-hexadecane) systems and thermodynamic modeling
ρ_l	937.17	kg/m³	333.15	Densities and Viscosities for the Ternary System of 1,2,3,4-Tetrahydronaphthalene + Isopropylcyclohexane + Cyclopropanemethanol and Corresponding Binaries at T = (293.15 to 343.15) K
ρ_l	933.19	kg/m³	338.15	Densities and Viscosities for the Ternary System of 1,2,3,4-Tetrahydronaphthalene + Isopropylcyclohexane + Cyclopropanemethanol and Corresponding Binaries at T = (293.15 to 343.15) K
ρ_l	929.10	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
ρ_l	929.20	kg/m³	343.15	Densities and Viscosities for the Ternary System of 1,2,3,4-Tetrahydronaphthalene + Isopropylcyclohexane + Cyclopropanemethanol and Corresponding Binaries at T = (293.15 to 343.15) K
ρ_l	920.90	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
ρ_l	912.90	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
ρ_l	904.80	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
Δ_fusS	[52.44; 52.44]	J/mol×K	[237.36; 237.36]
Δ_fusS	52.44	J/mol×K	237.36	NIST
Δ_fusS	52.44	J/mol×K	237.36	NIST

Datasets

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
298.15	100.00	0.0020
298.15	40300.00	0.0029
298.15	78600.00	0.0042
298.15	80900.00	0.0042
298.15	119800.00	0.0060
298.15	120600.00	0.0060
298.15	158900.00	0.0085
298.15	190200.00	0.0112
298.15	100.00	0.0020
323.15	100.00	0.0013
323.15	39900.00	0.0018
323.15	80300.00	0.0026
323.15	80600.00	0.0026
323.15	120900.00	0.0035
323.15	121000.00	0.0035
323.15	161200.00	0.0047
323.15	190600.00	0.0058
323.15	100.00	0.0013
348.15	100.00	0.0009
348.15	41000.00	0.0013
348.15	79700.00	0.0017
348.15	80600.00	0.0017
348.15	119500.00	0.0023
348.15	121700.00	0.0023
348.15	163000.00	0.0030
348.15	190800.00	0.0036
348.15	100.00	0.0009
373.15	100.00	0.0007
373.15	40500.00	0.0010
373.15	80300.00	0.0013
373.15	81100.00	0.0013
373.15	122500.00	0.0017
373.15	123000.00	0.0017
373.15	160200.00	0.0021
373.15	190600.00	0.0025
373.15	100.00	0.0007
398.15	100.00	0.0005
398.15	40500.00	0.0008
398.15	80600.00	0.0010
398.15	81800.00	0.0010
398.15	120800.00	0.0013
398.15	159900.00	0.0016
398.15	161000.00	0.0016
398.15	200600.00	0.0020
398.15	100.00	0.0005
423.15	100.00	0.0004
423.15	40500.00	0.0006
423.15	81000.00	0.0008
423.15	82200.00	0.0008
423.15	120800.00	0.0010
423.15	160800.00	0.0013
423.15	161300.00	0.0013
423.15	201000.00	0.0015
423.15	100.00	0.0004
448.15	100.00	0.0004
448.15	40400.00	0.0005
448.15	80400.00	0.0007
448.15	81200.00	0.0007
448.15	120200.00	0.0008
448.15	160600.00	0.0010
448.15	161200.00	0.0010
448.15	200100.00	0.0012
448.15	100.00	0.0004
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
P_vap	[1.33; 202.65]	kPa	[352.27; 525.05]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.38270e+01
Coefficient B			-3.96508e+03
Coefficient C			-5.94180e+01
Temperature range, min.			352.27
Temperature range, max.			525.05

P_vap	1.33	kPa	352.27	Calculated Property
P_vap	3.07	kPa	371.47	Calculated Property
P_vap	6.40	kPa	390.67	Calculated Property
P_vap	12.34	kPa	409.86	Calculated Property
P_vap	22.20	kPa	429.06	Calculated Property
P_vap	37.71	kPa	448.26	Calculated Property
P_vap	60.92	kPa	467.46	Calculated Property
P_vap	94.27	kPa	486.65	Calculated Property
P_vap	140.51	kPa	505.85	Calculated Property
P_vap	202.65	kPa	525.05	Calculated Property
P_vap	[1.38e-04; 3626.24]	kPa	[237.40; 720.15]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + Cln(T) + DT^2
Coefficient A			9.13922e+01
Coefficient B			-9.58531e+03
Coefficient C			-1.10009e+01
Coefficient D			4.80933e-06
Temperature range, min.			237.40
Temperature range, max.			720.15

P_vap	1.38e-04	kPa	237.40	Calculated Property
P_vap	0.03	kPa	291.04	Calculated Property
P_vap	0.89	kPa	344.68	Calculated Property
P_vap	9.26	kPa	398.32	Calculated Property
P_vap	49.94	kPa	451.96	Calculated Property
P_vap	176.64	kPa	505.59	Calculated Property
P_vap	472.46	kPa	559.23	Calculated Property
P_vap	1046.14	kPa	612.87	Calculated Property
P_vap	2035.67	kPa	666.51	Calculated Property
P_vap	3626.24	kPa	720.15	Calculated Property

Similar Compounds

Naphthalene, 1,2,3,4-tetrahydro-6-methyl-.

Naphthalene, 1,2,3,4-tetrahydro-5-methyl-.

Naphthalene, 1,2,3,4-tetrahydro-6-propyl-.

Naphthalene, 6-butyl-1,2,3,4-tetrahydro-.

Naphthalene, 6-ethyl-1,2,3,4-tetrahydro-.

Find more compounds similar to Naphthalene, 1,2,3,4-tetrahydro-.

Mixtures

Find more mixtures with Naphthalene, 1,2,3,4-tetrahydro-.

Sources

KDB Vapor Pressure Data
Crippen Method
Experimental measurement and thermodynamic modeling of phase equilibria of {CO2 + tetralin + n-alkanes (with n = 6, 16)} and its binary systems
Densities, sound velocities, and refractive indexes of (tetralin + n-decane) and thermodynamic modeling by Prigogine-Flory-Patterson model
Thermodynamic modeling and experimental speeds of sound, densities, and refractive indexes of (tetralin + n-dodecane)
Experimental high pressure speed of sound and density of (tetralin + n-decane) and (tetralin + n-hexadecane) systems and thermodynamic modeling
Excess volumes, densities, speeds of sound and viscosities for the binary systems of diisopropyl ether with hydrocarbons at 303.15K
Prediction and Experimental Measurement of Refractive Index in Ternary Hydrocarbon Mixtures
Mass Diffusion Coefficient and Soret Coefficient of o-Dichlorobenzene Solutions of PCBM and [60]Fullerene by the Soret Forced Rayleigh Scattering Method
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
Measurement and Correlation of the Solubilities of Sulfur S8 in 10 Solvents
Liquid-Liquid Equilibria of Formic Acid and Furfural in a Biphasic Aqueous-Organic System: Optimization of Solvent and Amine Extractant
Densities and Viscosities for the Ternary System of 1,2,3,4-Tetrahydronaphthalene + Isopropylcyclohexane + Cyclopropanemethanol and Corresponding Binaries at T = (293.15 to 343.15) K
Mutual Solubilities for Water-o-Nitrotoluene System and Distribution Coefficients for Furfural and Acetic Acid in Water-o-Nitrotoluene System
Densities, Sound Velocities, and Refractive Indexes of Tetralin + n-Hexadecane at (293.15, 303.15, 313.15, 323.15, 333.15, and 343.15) K
Densities, Viscosities, and Refractive Indices of Binary Mixtures of 1,2,3,4-Tetrahydronaphthalene with Some n-Alkanes at T = (293.15 to 313.15) K
Viscosity and Density of Five Hydrocarbon Liquids at Pressures up to 200 MPa and Temperatures up to 473 K
Comparison between Experimental and Theoretical Estimations of the Thermal Expansion, Concentration Expansion Coefficients, and Viscosity for Binary Mixtures under Pressures up to 20 MPa
Joback Method
KDB
Aqueous Solubility Prediction 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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Chemical Properties of Naphthalene, 1,2,3,4-tetrahydro- (CAS 119-64-2)