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

Naphthalene, 1,2,3,4-tetrahydro-

InChI
InChI=1S/C10H12/c1-2-6-10-8-4-3-7-9(10)5-1/h1-2,5-6H,3-4,7-8H2
InChI Key
CXWXQJXEFPUFDZ-UHFFFAOYSA-N
Formula
C10H12
SMILES
c1ccc2c(c1)CCCC2
Molecular Weight1
132.20
CAS
119-64-2
Other Names
  • 1,2,3,4-tetrahydronaphthalene
  • Bacticin
  • Benzocyclohexane
  • NSC 77451
  • Naphthalene-1,2,3,4-tetrahydride
  • Tetrahydronaphthalene
  • Tetralina
  • Tetraline
  • Tetranap
  • tetralene
  • tetralin
  • «delta»(5,7,9)-Naphthantriene
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Physical Properties

Property Value Unit Source
ω [0.3028; 0.3207]   Show Hide
ω 0.3207 PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω 0.3028 Passut and Danner (1973), critical constants and acentric factors Compiled value
ω 0.3030 KDB
PAff [800.80; 809.70] kJ/mol Show Hide
PAff 809.70 kJ/mol NIST
PAff 800.80 kJ/mol NIST
BasG [774.00; 782.10] kJ/mol Show Hide
BasG 782.10 kJ/mol NIST
BasG 774.00 kJ/mol NIST
ΔcH°liquid [-5621.54; -5581.90] kJ/mol Show Hide
ΔcH°liquid -5621.54 ± 0.88 kJ/mol NIST
ΔcH°liquid -5617.50 ± 2.10 kJ/mol NIST
ΔcH°liquid -5598.60 kJ/mol NIST
ΔcH°liquid -5581.90 kJ/mol NIST
ΔfG° 167.10 kJ/mol KDB
ΔfH°gas [2.76; 30.00] kJ/mol Show Hide
ΔfH°gas 2.76 kJ/mol KDB
ΔfH°gas 30.00 kJ/mol NIST
ΔfH°gas 26.00 ± 2.00 kJ/mol NIST
ΔfH°liquid [-32.60; -28.60] kJ/mol Show Hide
ΔfH°liquid -28.60 ± 1.00 kJ/mol NIST
ΔfH°liquid -32.60 ± 2.20 kJ/mol NIST
ΔfusH° 10.27 kJ/mol Joback Calculated Property
ΔvapH° [55.00; 58.60] kJ/mol Show Hide
ΔvapH° 55.00 ± 1.00 kJ/mol NIST
ΔvapH° 58.60 kJ/mol NIST
IE [8.44; 9.14] eV Show Hide
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
logPoct/wat 2.565 Crippen Calculated Property
McVol 117.140 ml/mol McGowan Calculated Property
NFPA Fire 2 KDB
NFPA Health 1 KDB
Pc [3514.95; 3750.00] kPa Show Hide
Pc 3650.00 kPa IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 3 Compiled value
Pc 3515.98 kPa PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc 3514.95 kPa Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc 3650.00 kPa KDB
Pc 3700.00 ± 100.00 kPa NIST
Pc 3630.00 ± 25.00 kPa NIST
Pc 3750.00 ± 80.00 kPa NIST
ρc [300.10; 330.51] kg/m3 Show Hide
ρc 330.51 ± 13.22 kg/m3 NIST
ρc 323.90 ± 6.61 kg/m3 NIST
ρc 300.10 ± 14.54 kg/m3 NIST
Inp [195.21; 1180.00]   Show Hide
Inp 1143.00 NIST
Inp 1143.00 NIST
Inp 1168.50 NIST
Inp 1142.80 NIST
Inp 1154.00 NIST
Inp 1180.00 NIST
Inp 1179.00 NIST
Inp 1170.00 NIST
Inp 1142.00 NIST
Inp 1142.00 NIST
Inp 1147.00 NIST
Inp 1136.00 NIST
Inp 1129.80 NIST
Inp 1164.00 NIST
Inp 1178.00 NIST
Inp 1137.00 NIST
Inp 1133.20 NIST
Inp 1137.60 NIST
Inp 1168.70 NIST
Inp 1179.80 NIST
Inp 1140.00 NIST
Inp 1142.00 NIST
Inp 1150.00 NIST
Inp 1155.00 NIST
Inp 1133.00 NIST
Inp 1137.00 NIST
Inp 1133.20 NIST
Inp 1137.60 NIST
Inp 1165.00 NIST
Inp 1168.00 NIST
Inp 1173.00 NIST
Inp 1140.00 NIST
Inp 1125.60 NIST
Inp 1150.00 NIST
Inp 1136.00 NIST
Inp 1163.35 NIST
Inp 1153.90 NIST
Inp 1151.70 NIST
Inp 1158.50 NIST
Inp 1162.50 NIST
Inp 1179.40 NIST
Inp 1142.90 NIST
Inp 1151.70 NIST
Inp 1158.50 NIST
Inp 1162.50 NIST
Inp 1140.47 NIST
Inp 1140.85 NIST
Inp 1141.00 NIST
Inp 1163.00 NIST
Inp 1130.46 NIST
Inp 1138.09 NIST
Inp 1142.95 NIST
Inp 1157.79 NIST
Inp 1166.27 NIST
Inp 1171.51 NIST
Inp 1136.00 NIST
Inp 1169.00 NIST
Inp 1133.00 NIST
Inp 1137.00 NIST
Inp 1142.00 NIST
Inp 1155.00 NIST
Inp 1147.00 NIST
Inp 1166.00 NIST
Inp 1169.00 NIST
Inp 1155.00 NIST
Inp 1148.00 NIST
Inp 1152.00 NIST
Inp 1162.00 NIST
Inp 1164.00 NIST
Inp 1174.00 NIST
Inp 1136.00 NIST
Inp 1147.00 NIST
Inp 1167.00 NIST
Inp 1137.00 NIST
Inp 1158.00 NIST
Inp 1171.00 NIST
Inp 1179.00 NIST
Inp 1137.00 NIST
Inp 1162.00 NIST
Inp 1163.00 NIST
Inp 1130.00 NIST
Inp 1144.00 NIST
Inp 1169.00 NIST
Inp 1142.10 NIST
Inp 1152.90 NIST
Inp 1149.70 NIST
Inp 1152.40 NIST
Inp 1141.00 NIST
Inp 1136.00 NIST
Inp 1153.00 NIST
Inp Outlier 195.21 NIST
Inp Outlier 195.47 NIST
Inp Outlier 197.04 NIST
Inp 1133.00 NIST
Inp 1166.00 NIST
Inp Outlier 195.21 NIST
Inp 1169.00 NIST
Inp 1164.00 NIST
Inp 1137.00 NIST
Ip [1476.00; 1565.00]   Show Hide
Ip 1490.40 NIST
Ip 1476.00 NIST
Ip 1523.00 NIST
Ip 1517.00 NIST
Ip 1565.00 NIST
Ip 1565.00 NIST
Ip 1490.00 NIST
Ip 1525.00 NIST
Ip 1525.00 NIST
Ip 1525.00 NIST
Ip 1523.00 NIST
S°liquid 251.46 J/mol×K NIST
Tboil [478.80; 484.15] K Show Hide
Tboil 481.45 K Excess volumes, densities, speeds of sound and viscosities for the binary systems of diisopropyl ether with hydrocarbons at 303.15K
Tboil 480.77 K KDB
Tboil 480.80 K NIST
Tboil Outlier 484.15 ± 5.00 K NIST
Tboil 480.45 ± 0.50 K NIST
Tboil 480.15 ± 0.50 K NIST
Tboil 480.56 ± 0.10 K NIST
Tboil 479.70 ± 1.00 K NIST
Tboil 478.80 ± 0.50 K NIST
Tc [719.20; 721.70] K Show Hide
Tc 720.00 K IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 3 Compiled value
Tc 719.20 K PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc 719.26 K Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc 720.00 K KDB
Tc 720.00 ± 1.00 K NIST
Tc 721.70 ± 0.50 K NIST
Tc 719.90 ± 1.00 K NIST
Tc 721.00 ± 1.50 K NIST
Tfus [236.45; 242.55] K Show Hide
Tfus 237.80 K Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus 237.40 K KDB
Tfus 238.73 K Aq. Solubility Prediction
Tfus Outlier 242.55 K NIST
Tfus 237.17 ± 0.20 K NIST
Tfus 237.31 ± 0.06 K NIST
Tfus 237.33 ± 0.04 K NIST
Tfus 237.36 ± 0.03 K NIST
Tfus 237.33 ± 0.20 K NIST
Tfus 236.45 ± 0.50 K NIST
Tfus 238.20 ± 0.60 K NIST
Ttriple [237.34; 237.35] K Show Hide
Ttriple 237.34 ± 0.07 K NIST
Ttriple 237.35 ± 0.05 K NIST
Ttriple 237.34 ± 0.07 K NIST
Ttriple 237.35 ± 0.05 K NIST
Vc [0.408; 0.408] m3/kmol Show Hide
Vc 0.408 m3/kmol IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 3 Compiled value
Vc 0.408 m3/kmol PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc 0.408 m3/kmol KDB
Vc 0.408 m3/kmol NIST
Zc [0.2487620; 0.2490000]   Show Hide
Zc 0.2490000 IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 3 Compiled value
Zc 0.2487620 KDB

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,liquid 217.44 J/mol×K 298.15 NIST
Csat [195.70; 227.90] J/mol×K [250.00; 320.00] Show Hide
Csat 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
Csat 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
Csat 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
Csat 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
Csat 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
Csat 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
Csat 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
Csat 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
Csat 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
Csat 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
ΔfusH [12.45; 12.45] kJ/mol [237.36; 237.40] Show Hide
ΔfusH 12.45 kJ/mol 237.36 NIST
ΔfusH 12.45 kJ/mol 237.36 NIST
ΔfusH 12.45 kJ/mol 237.40 NIST
ΔfusH 12.45 kJ/mol 237.40 NIST
ΔvapH [32.00; 52.10] kJ/mol [384.00; 604.00] Show Hide
ΔvapH 52.10 kJ/mol 384.00 NIST
ΔvapH 51.10 kJ/mol 396.00 NIST
ΔvapH 48.60 kJ/mol 423.00 NIST
ΔvapH 41.30 ± 0.10 kJ/mol 498.00 NIST
ΔvapH 44.10 kJ/mol 522.50 NIST
ΔvapH 37.60 ± 0.10 kJ/mol 552.00 NIST
ΔvapH 35.70 ± 0.10 kJ/mol 567.00 NIST
ΔvapH 33.90 ± 0.10 kJ/mol 585.00 NIST
ΔvapH 32.00 ± 0.10 kJ/mol 604.00 NIST
n0 [1.51790; 1.54155]   [293.15; 343.15] Show Hide
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
ρl [904.80; 973.00] kg/m3 [293.00; 373.15] Show Hide
ρl 973.00 kg/m3 293.00 KDB
ρl 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
ρl 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
ρl 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
ρl 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
ρl 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
ρl 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
ρl 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
ρl 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
ρl 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
ρl 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
ρl 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
ρl 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
ρl 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
ρl 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
ρl 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
ρl 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
ρl 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
ρl 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
ρl 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
ρl 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
ρl 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
ρl 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
ρl 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
ΔfusS [52.44; 52.44] J/mol×K [237.36; 237.36] Show Hide
ΔfusS 52.44 J/mol×K 237.36 NIST
ΔfusS 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
Cp,gas [132.31; 388.53] J/mol×K [273.00; 1000.00] Joback Predicted correlation Show Hide
EquationY = A + B·T + C·T² + D·T³ + E·T⁴
Y is Cp,gas in J/mol×K, T in K
Coefficient A-8.71100e+01
Coefficient B9.83200e-01
Coefficient C-7.13560e-04
Coefficient D2.06000e-07
Coefficient E0.00000e+00
Temperature range, min.273.00
Temperature range, max.1000.00
Cp,gas 132.31 J/mol×K 273.00 Calculated Property
Cp,gas 180.54 J/mol×K 353.78 Calculated Property
Cp,gas 222.30 J/mol×K 434.56 Calculated Property
Cp,gas 258.26 J/mol×K 515.33 Calculated Property
Cp,gas 289.06 J/mol×K 596.11 Calculated Property
Cp,gas 315.36 J/mol×K 676.89 Calculated Property
Cp,gas 337.80 J/mol×K 757.67 Calculated Property
Cp,gas 357.04 J/mol×K 838.44 Calculated Property
Cp,gas 373.74 J/mol×K 919.22 Calculated Property
Cp,gas 388.53 J/mol×K 1000.00 Calculated Property
Property Value Unit Temperature (K) Source
η [0.0039746; 0.0002876] Pa×s [237.51; 504.09] Joback Predicted correlation Show Hide
EquationY = exp(A + B/T + C·ln(T) + D·T^E)
Y is η in Pa×s, T in K
Coefficient A-1.04936e+01
Coefficient B1.17942e+03
Coefficient C0.00000e+00
Coefficient D0.00000e+00
Coefficient E0.00000e+00
CommentLiquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc.
Temperature range, min.237.51
Temperature range, max.504.09
η 0.0039746 Pa×s 237.51 Calculated Property
η 0.0022917 Pa×s 267.13 Calculated Property
η 0.0014749 Pa×s 296.75 Calculated Property
η 0.0010283 Pa×s 326.37 Calculated Property
η 0.0007612 Pa×s 355.99 Calculated Property
η 0.0005902 Pa×s 385.61 Calculated Property
η 0.0004745 Pa×s 415.23 Calculated Property
η 0.0003927 Pa×s 444.85 Calculated Property
η 0.0003328 Pa×s 474.47 Calculated Property
η 0.0002876 Pa×s 504.09 Calculated Property
Property Value Unit Temperature (K) Source
Pvap [1.33; 202.65] kPa [352.27; 525.05] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.38270e+01
Coefficient B-3.96508e+03
Coefficient C-5.94180e+01
Temperature range, min.352.27
Temperature range, max.525.05
Pvap 1.33 kPa 352.27 Calculated Property
Pvap 3.07 kPa 371.47 Calculated Property
Pvap 6.40 kPa 390.67 Calculated Property
Pvap 12.34 kPa 409.86 Calculated Property
Pvap 22.20 kPa 429.06 Calculated Property
Pvap 37.71 kPa 448.26 Calculated Property
Pvap 60.92 kPa 467.46 Calculated Property
Pvap 94.27 kPa 486.65 Calculated Property
Pvap 140.51 kPa 505.85 Calculated Property
Pvap 202.65 kPa 525.05 Calculated Property
Pvap [1.38e-04; 3626.24] kPa [237.40; 720.15] KDB Vapor Pressure Data Show Hide
Equationln(Y) = A + B/T + C·ln(T) + D·T² + E/T²
Y is Pvap in kPa, T in K
Coefficient A9.13922e+01
Coefficient B-9.58531e+03
Coefficient C-1.10009e+01
Coefficient D4.80933e-06
Coefficient E0.00000e+00
Temperature range, min.237.40
Temperature range, max.720.15
Pvap 1.38e-04 kPa 237.40 Calculated Property
Pvap 0.03 kPa 291.04 Calculated Property
Pvap 0.89 kPa 344.68 Calculated Property
Pvap 9.26 kPa 398.32 Calculated Property
Pvap 49.94 kPa 451.96 Calculated Property
Pvap 176.64 kPa 505.59 Calculated Property
Pvap 472.46 kPa 559.23 Calculated Property
Pvap 1046.14 kPa 612.87 Calculated Property
Pvap 2035.67 kPa 666.51 Calculated Property
Pvap 3626.24 kPa 720.15 Calculated Property
Pvap [2.69; 98.67] kPa [367.00; 479.40] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.41073e+01
Coefficient B-3.89347e+03
Coefficient C-7.02290e+01
ReferenceHerz and Schuftan, 1922
CommentCoefficents calculated by NIST from author's data.
Temperature range, min.367.00
Temperature range, max.479.40
Pvap 2.69 kPa 367.00 Calculated Property
Pvap 4.56 kPa 379.49 Calculated Property
Pvap 7.44 kPa 391.98 Calculated Property
Pvap 11.69 kPa 404.47 Calculated Property
Pvap 17.78 kPa 416.96 Calculated Property
Pvap 26.27 kPa 429.44 Calculated Property
Pvap 37.81 kPa 441.93 Calculated Property
Pvap 53.15 kPa 454.42 Calculated Property
Pvap 73.13 kPa 466.91 Calculated Property
Pvap 98.67 kPa 479.40 Calculated Property
Property Value Unit Temperature (K) Source
γ [0.04; 0.02] N/m [237.35; 480.75] Jasper (1972), surface tension of pure liquid compounds Compiled value Show Hide
EquationY = A + B·T + C·T² + D·T³ + E·T⁴
Y is γ in N/m, T in K
Coefficient A6.16085e-02
Coefficient B-9.54000e-05
Coefficient C0.00000e+00
Coefficient D0.00000e+00
Coefficient E0.00000e+00
Temperature range, min.237.35
Temperature range, max.480.75
γ 0.04 N/m 237.35 Calculated Property
γ 0.04 N/m 264.39 Calculated Property
γ 0.03 N/m 291.44 Calculated Property
γ 0.03 N/m 318.48 Calculated Property
γ 0.03 N/m 345.53 Calculated Property
γ 0.03 N/m 372.57 Calculated Property
γ 0.02 N/m 399.62 Calculated Property
γ 0.02 N/m 426.66 Calculated Property
γ 0.02 N/m 453.71 Calculated Property
γ 0.02 N/m 480.75 Calculated Property

Similar Compounds

1,2,3,4-Tetrahydronaphthalene-d12. Benzene, 1,2-dibutyl. Benzene, 1-butyl-2-propyl. Benzene, 1-butyl-2-ethyl-. Benzene, 1-butyl-2-methyl-. Benzocycloheptene. Benzene, 1,2-dipentyl. Naphthalene, 1,2,3,4-tetrahydro-6-methyl-. Naphthalene, 1,2,3,4-tetrahydro-5-methyl-. Benzene, 1-butyl-2-pentyl. Naphthalene, 1,2,3,4-tetrahydro-6-propyl-. Benzene, 1-ethyl-2-pentyl. Benzene, 1-pentyl-2-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

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Sources

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