Chemical Properties of Nonane (CAS 111-84-2)

Nonane

InChI
InChI=1S/C9H20/c1-3-5-7-9-8-6-4-2/h3-9H2,1-2H3
InChI Key
BKIMMITUMNQMOS-UHFFFAOYSA-N
Formula
C9H20
SMILES
CCCCCCCCC
Molecular Weight1
128.26
CAS
111-84-2
Other Names
  • Shellsol 140
  • UN 1920
  • n-C9H20
  • n-nonane
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Contents

  1. Physical Properties
  2. Temperature Dependent Properties
  3. Datasets
  4. Correlations
  5. Similar Compounds
  6. Mixtures
  7. Sources

Physical Properties

Property Value Unit Source
ω [0.4430; 0.4450]   Show Hide
ω 0.4440 PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω 0.4437 Passut and Danner (1973), critical constants and acentric factors Compiled value
ω 0.4430 ChemSep v8.3 pure component data Compiled value
ω 0.4450 KDB
Tig 478.15 K KDB
AP 346.850 K KDB
ΔcH°liquid [-6125.21; -6119.80] kJ/mol Show Hide
ΔcH°liquid -6125.21 ± 0.54 kJ/mol NIST
ΔcH°liquid -6124.90 ± 1.10 kJ/mol NIST
ΔcH°liquid -6119.80 kJ/mol NIST
μ 0.00 debye ChemSep v8.3 pure component data Compiled value
LFL 0.87 % in Air KDB
UFL 2.90 % in Air KDB
Tflash,oc 304.26 K KDB
ΔfG° [24.83; 24.98] kJ/mol Show Hide
ΔfG° 24.98 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfG° 24.83 kJ/mol KDB
Δc,grossH 6125.17 kJ/mol KDB
Δc,netH 5685.052 kJ/mol KDB
ΔfH°gas [-229.20; -228.30] kJ/mol Show Hide
ΔfH°gas -228.74 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfH°gas -229.20 kJ/mol KDB
ΔfH°gas -228.30 kJ/mol NIST
ΔfH°liquid -274.70 ± 1.00 kJ/mol NIST
ΔfusH° 19.07 kJ/mol Joback Calculated Property
ΔvapH° [46.40; 46.60] kJ/mol Show Hide
ΔvapH° 46.43 kJ/mol NIST
ΔvapH° 46.50 ± 0.20 kJ/mol NIST
ΔvapH° 46.60 ± 0.20 kJ/mol NIST
ΔvapH° 46.60 kJ/mol NIST
ΔvapH° 46.40 kJ/mol NIST
ΔvapH° 46.40 kJ/mol NIST
ΔvapH° 46.43 kJ/mol NIST
IE [9.63; 10.19] eV Show Hide
IE 9.71 ± 0.10 eV NIST
IE 9.87 eV NIST
IE 9.71 ± 0.10 eV NIST
IE 9.63 ± 0.15 eV NIST
IE 10.19 eV NIST
log10WS [-5.88; -5.88]   Show Hide
log10WS -5.88 Aq. Solubility Prediction
log10WS -5.88 Estimated Solubility
logPoct/wat 3.757 Crippen Calculated Property
McVol 137.670 ml/mol McGowan Calculated Property
NFPA Fire 3 KDB
Pc [2270.00; 2357.30] kPa Show Hide
Pc 2290.00 kPa IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Pc 2279.81 kPa PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc 2289.06 kPa Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc 2290.00 kPa ChemSep v8.3 pure component data Compiled value
Pc 2290.00 kPa KDB
Pc 2290.00 ± 50.00 kPa NIST
Pc 2280.00 ± 20.00 kPa NIST
Pc 2299.00 ± 5.00 kPa NIST
Pc 2270.00 ± 30.00 kPa NIST
Pc 2291.10 ± 0.22 kPa NIST
Pc 2290.40 ± 0.22 kPa NIST
Pc 2305.60 ± 0.23 kPa NIST
Pc Outlier 2357.30 ± 0.23 kPa NIST
Pc 2294.00 ± 6.89 kPa NIST
Pc 2288.00 ± 10.00 kPa NIST
Ptriple 4.31e-04 kPa ChemSep v8.3 pure component data Compiled value
ρc [230.86; 235.99] kg/m3 Show Hide
ρc 230.86 ± 6.41 kg/m3 NIST
ρc 235.99 ± 10.00 kg/m3 NIST
ρc 230.86 ± 6.41 kg/m3 NIST
Inp [138.27; 144.03]   Show Hide
Inp 138.27 NIST
Inp 144.03 NIST
Inp 138.27 NIST
S°gas 506.50 ± 1.00 J/mol×K NIST
S°liquid [392.90; 393.67] J/mol×K Show Hide
S°liquid 393.67 J/mol×K NIST
S°liquid 392.90 J/mol×K NIST
Tboil [421.15; 424.15] K Show Hide
Tboil 423.80 K Isobaric vapor-liquid equilibrium for the binary mixtures of nonane with cyclohexane, toluene, m-xylene, or p-xylene at 101.3 kPa
Tboil 423.80 K Isobaric vapor-liquid equilibrium for binary systemsof toluene + o-xylene, benzene + o-xylene, nonane + benzene and nonane + heptane at 101.3 kPa
Tboil 423.94 K Solutions of alkyl methanoates and alkanes: Simultaneous modeling of phase equilibria and mixing properties. Estimation of behavior by UNIFAC with recalculation of parameters
Tboil 423.66 K Densities and Excess Molar Properties of Dimethyl Carbonate with Alkanes (C6 to C10) and VLE of Dimethyl Carbonate with Alkanes (C9 to C10) at 101.3 kPa
Tboil 423.97 K Isobaric Vapor-Liquid Equilibria of the Ternary System Methylbutyl Ketone + Nonane + Cyclohexanol
Tboil 423.94 K Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Tboil 423.97 K ChemSep v8.3 pure component data Compiled value
Tboil 423.97 K KDB
Tboil 424.00 K NIST
Tboil 424.00 K NIST
Tboil 423.82 ± 0.25 K NIST
Tboil 423.88 ± 0.50 K NIST
Tboil 424.15 ± 0.20 K NIST
Tboil 423.90 ± 0.50 K NIST
Tboil 423.54 ± 0.50 K NIST
Tboil 423.20 ± 2.00 K NIST
Tboil 423.75 ± 0.30 K NIST
Tboil 423.91 ± 0.15 K NIST
Tboil 423.45 ± 0.40 K NIST
Tboil 423.45 ± 0.17 K NIST
Tboil 423.85 ± 0.20 K NIST
Tboil 423.45 ± 0.25 K NIST
Tboil 423.95 ± 0.15 K NIST
Tboil 423.65 ± 0.25 K NIST
Tboil 423.95 ± 0.30 K NIST
Tboil Outlier 421.65 ± 1.50 K NIST
Tboil 423.75 ± 0.50 K NIST
Tboil 423.80 ± 0.60 K NIST
Tboil 423.80 ± 0.20 K NIST
Tboil 423.80 ± 0.20 K NIST
Tboil 422.95 ± 0.50 K NIST
Tboil 423.92 ± 0.15 K NIST
Tboil 423.86 ± 0.50 K NIST
Tboil 423.90 ± 0.30 K NIST
Tboil 423.94 ± 0.03 K NIST
Tboil 423.05 ± 1.00 K NIST
Tboil 423.96 ± 0.30 K NIST
Tboil 423.95 ± 0.30 K NIST
Tboil 423.94 ± 0.01 K NIST
Tboil 424.00 ± 0.15 K NIST
Tboil 424.00 ± 2.00 K NIST
Tboil 423.65 ± 2.00 K NIST
Tboil 424.00 ± 0.20 K NIST
Tboil 423.95 ± 0.10 K NIST
Tboil 423.85 ± 0.60 K NIST
Tboil 423.85 ± 0.30 K NIST
Tboil 423.96 ± 0.20 K NIST
Tboil 423.40 ± 0.70 K NIST
Tboil 423.85 ± 0.30 K NIST
Tboil 423.70 ± 0.50 K NIST
Tboil 423.87 ± 0.10 K NIST
Tboil 423.86 ± 0.15 K NIST
Tboil 423.88 ± 0.10 K NIST
Tboil 423.86 ± 0.15 K NIST
Tboil 423.87 ± 0.10 K NIST
Tboil Outlier 421.15 ± 3.00 K NIST
Tboil 423.90 ± 2.00 K NIST
Tboil 422.65 ± 0.70 K NIST
Tboil 422.65 ± 1.00 K NIST
Tc [593.61; 595.85] K Show Hide
Tc 594.52 K Experimental determination of critical data of multi-component mixtures containing potential gasoline additives 2-butanol by a flow-type apparatus
Tc 594.50 K Measurement of Critical Properties for Binary and Ternary Mixtures Containing n-Butanol and n-Alkane
Tc 594.52 K Determination of the Critical Properties of C6 C10 n-Alkanes and Their Binary Systems Using a Flow Apparatus
Tc 594.60 K IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Tc 594.70 K PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc 594.64 K Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc 594.60 K ChemSep v8.3 pure component data Compiled value
Tc 594.60 K KDB
Tc 594.60 ± 0.60 K NIST
Tc 594.60 ± 1.00 K NIST
Tc 594.50 ± 0.30 K NIST
Tc 594.70 ± 0.60 K NIST
Tc 594.60 K NIST
Tc 593.81 ± 0.10 K NIST
Tc 594.60 ± 0.40 K NIST
Tc 594.60 K NIST
Tc 594.60 ± 0.70 K NIST
Tc 593.61 ± 0.20 K NIST
Tc Outlier 595.85 ± 0.05 K NIST
Tc Outlier 595.85 ± 0.05 K NIST
Tc 595.65 ± 0.05 K NIST
Tc 595.75 ± 0.05 K NIST
Tc 593.80 ± 0.30 K NIST
Tc 594.56 ± 0.10 K NIST
Tfus [218.95; 220.15] K Show Hide
Tfus 219.90 K Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus 219.66 K ChemSep v8.3 pure component data Compiled value
Tfus 219.60 K KDB
Tfus 219.77 K Aq. Solubility Prediction
Tfus 219.56 ± 0.02 K NIST
Tfus 219.85 ± 0.15 K NIST
Tfus 219.64 ± 0.20 K NIST
Tfus 219.60 ± 0.20 K NIST
Tfus 219.61 ± 0.08 K NIST
Tfus 219.45 ± 0.20 K NIST
Tfus 219.62 ± 0.08 K NIST
Tfus Outlier 218.95 ± 0.50 K NIST
Tfus Outlier 218.95 ± 0.60 K NIST
Tfus 219.61 ± 0.02 K NIST
Tfus 219.54 ± 0.01 K NIST
Tfus 219.19 ± 0.20 K NIST
Tfus 219.35 ± 0.40 K NIST
Tfus 219.45 ± 0.40 K NIST
Tfus 219.35 ± 0.20 K NIST
Tfus 219.45 ± 0.20 K NIST
Tfus Outlier 220.15 ± 2.00 K NIST
Tfus 219.45 ± 0.10 K NIST
Tfus 219.20 ± 0.30 K NIST
Tfus 219.25 ± 0.40 K NIST
Tfus 219.47 ± 0.08 K NIST
Tfus 219.50 ± 0.12 K NIST
Tfus 219.39 ± 0.15 K NIST
Tfus 219.45 ± 0.10 K NIST
Ttriple [219.20; 219.66] K Show Hide
Ttriple 219.66 K ChemSep v8.3 pure component data Compiled value
Ttriple 219.65 K KDB
Ttriple 219.65 ± 0.01 K NIST
Ttriple 219.65 ± 0.03 K NIST
Ttriple 219.65 ± 0.20 K NIST
Ttriple 219.62 ± 0.20 K NIST
Ttriple 219.62 ± 0.06 K NIST
Ttriple 219.62 ± 0.03 K NIST
Ttriple Outlier 219.20 ± 0.20 K NIST
UQi 5.48 ChemSep v8.3 pure component data Compiled value
URi 6.52 ChemSep v8.3 pure component data Compiled value
Vc [0.555; 0.555] m3/kmol Show Hide
Vc 0.555 m3/kmol IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Vc 0.555 m3/kmol PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc 0.555 m3/kmol ChemSep v8.3 pure component data Compiled value
Vc 0.555 m3/kmol KDB
Vc 0.555 m3/kmol NIST
VCOSTALD 0.55 m3/kmol Hankinson and Thomson (1979), COSTALD parameters Compiled value
ωSRK 0.45 Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zc [0.2570000; 0.2570790]   Show Hide
Zc 0.2570000 IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Zc 0.2570000 ChemSep v8.3 pure component data Compiled value
Zc 0.2570790 KDB
Zra [0.25; 0.25]   Show Hide
Zra 0.25 Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zra 0.25 ChemSep v8.3 pure component data Compiled value
Zra 0.25 KDB

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,liquid [264.50; 323.20] J/mol×K [230.00; 370.00] Show Hide
Cp,liquid 264.50 J/mol×K 230.00 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 265.10 J/mol×K 240.00 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 266.90 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 269.50 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 272.90 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 274.00 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 276.70 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 280.13 J/mol×K 288.15 Thermodynamic behaviour of the binary systems dimethyl carbonate + n-octane or n-nonane
Cp,liquid 280.90 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 280.70 J/mol×K 297.90 NIST
Cp,liquid 284.34 J/mol×K 298.15 NIST
Cp,liquid 284.76 J/mol×K 298.15 NIST
Cp,liquid 284.00 J/mol×K 298.15 NIST
Cp,liquid 283.80 J/mol×K 298.15 NIST
Cp,liquid 284.40 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 284.23 J/mol×K 298.15 Thermodynamic behaviour of the binary systems dimethyl carbonate + n-octane or n-nonane
Cp,liquid 284.01 J/mol×K 298.15 NIST
Cp,liquid 284.39 J/mol×K 298.15 NIST
Cp,liquid 281.20 J/mol×K 299.10 NIST
Cp,liquid 285.20 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 288.80 J/mol×K 308.15 Thermodynamic behaviour of the binary systems dimethyl carbonate + n-octane or n-nonane
Cp,liquid 289.50 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 292.18 J/mol×K 318.15 NIST
Cp,liquid 293.90 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
Cp,liquid 293.20 J/mol×K 323.00 NIST
Cp,liquid 298.50 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 303.60 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 322.20 J/mol×K 350.00 NIST
Cp,liquid 309.30 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 315.80 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 323.20 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
η [0.0003460; 0.0009720] Pa×s [273.15; 358.15] Show Hide
η 0.0009720 Pa×s 273.15 Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
η 0.0008960 Pa×s 278.15 Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
η 0.0008280 Pa×s 283.15 Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
η 0.0007680 Pa×s 288.15 Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
η 0.0007091 Pa×s 293.15 Densities and Viscosities of Ternary Mixtures of Heptane, Octane, Nonane, and Hexyl Benzene from 293.15 K to 313.15 K
η 0.0007160 Pa×s 293.15 Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
η 0.0006690 Pa×s 298.15 Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
η 0.0006640 Pa×s 298.15 Densities and Viscosities of Ternary Mixtures of Heptane, Octane, Nonane, and Hexyl Benzene from 293.15 K to 313.15 K
η 0.0006217 Pa×s 303.15 Densities and Viscosities of Ternary Mixtures of Heptane, Octane, Nonane, and Hexyl Benzene from 293.15 K to 313.15 K
η 0.0006280 Pa×s 303.15 Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
η 0.0005849 Pa×s 308.15 Densities and Viscosities of Ternary Mixtures of Heptane, Octane, Nonane, and Hexyl Benzene from 293.15 K to 313.15 K
η 0.0005900 Pa×s 308.15 Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
η 0.0005500 Pa×s 313.15 Densities and Viscosities of Ternary Mixtures of Heptane, Octane, Nonane, and Hexyl Benzene from 293.15 K to 313.15 K
η 0.0005550 Pa×s 313.15 Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
η 0.0005220 Pa×s 318.15 Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
η 0.0004930 Pa×s 323.15 Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
η 0.0004660 Pa×s 328.15 Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
η 0.0004420 Pa×s 333.15 Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
η 0.0004200 Pa×s 338.15 Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
η 0.0003990 Pa×s 343.15 Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
η 0.0003800 Pa×s 348.15 Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
η 0.0003620 Pa×s 353.15 Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
η 0.0003460 Pa×s 358.15 Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
εr [1.93; 1.99]   [288.15; 338.15] Show Hide
εr 1.99 288.15 Study of static permittivity and density of the systems {(n-nonane + monoglyme or diglyme)} at various temperatures
εr 1.98 298.15 Study of static permittivity and density of the systems {(n-nonane + monoglyme or diglyme)} at various temperatures
εr 1.97 308.15 Study of static permittivity and density of the systems {(n-nonane + monoglyme or diglyme)} at various temperatures
εr 1.95 318.15 Study of static permittivity and density of the systems {(n-nonane + monoglyme or diglyme)} at various temperatures
εr 1.94 328.15 Study of static permittivity and density of the systems {(n-nonane + monoglyme or diglyme)} at various temperatures
εr 1.93 338.15 Study of static permittivity and density of the systems {(n-nonane + monoglyme or diglyme)} at various temperatures
ΔfusH [15.00; 15.48] kJ/mol [219.50; 219.70] Show Hide
ΔfusH 15.00 kJ/mol 219.50 NIST
ΔfusH 15.48 kJ/mol 219.70 NIST
ΔsubH 74.60 kJ/mol 219.00 NIST
ΔvapH [36.91; 48.30] kJ/mol [263.50; 424.00] Show Hide
ΔvapH 48.30 kJ/mol 263.50 NIST
ΔvapH 46.70 kJ/mol 299.00 NIST
ΔvapH 46.00 kJ/mol 314.00 NIST
ΔvapH 44.30 kJ/mol 328.00 NIST
ΔvapH 43.20 kJ/mol 343.00 NIST
ΔvapH 42.10 kJ/mol 358.00 NIST
ΔvapH 43.90 kJ/mol 367.50 NIST
ΔvapH 42.70 kJ/mol 385.00 NIST
ΔvapH 36.91 kJ/mol 423.80 KDB
ΔvapH 36.91 kJ/mol 424.00 NIST
Pvap [2.34; 195.54] kPa [322.59; 450.56] Show Hide
Pvap 2.34 kPa 322.59 Vapor-Liquid Equilibrium Studies for Systems Containing n-Butylisocyanate at Temperatures between 323.15 K and 371.15 K
Pvap 3.97 kPa 333.15 Vapor liquid equilibria and density measurement for binary mixtures of toluene, benzene, o-xylene, m-xylene, sulfolane and nonane at 333.15K and 353.15K
Pvap 4.99 kPa 338.33 Vapor-Liquid Equilibrium Studies for Systems Containing n-Butylisocyanate at Temperatures between 323.15 K and 371.15 K
Pvap 9.00 kPa 351.53 Vapor-Liquid Equilibrium Studies for Systems Containing n-Butylisocyanate at Temperatures between 323.15 K and 371.15 K
Pvap 9.65 kPa 353.15 Measurement of vapor.liquid equilibria (VLE) and excess enthalpies (HE) of binary systems with 1-alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide and prediction of these properties and A using modified UNIFAC (Dortmund)
Pvap 10.28 kPa 353.15 Vapor liquid equilibria and density measurement for binary mixtures of toluene, benzene, o-xylene, m-xylene, sulfolane and nonane at 333.15K and 353.15K
Pvap 15.58 kPa 365.30 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 18.07 kPa 369.25 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 19.81 kPa 371.37 Vapor-Liquid Equilibrium Studies for Systems Containing n-Butylisocyanate at Temperatures between 323.15 K and 371.15 K
Pvap 20.58 kPa 372.81 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 23.49 kPa 376.46 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 26.35 kPa 379.71 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 28.78 kPa 382.25 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 31.22 kPa 384.65 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 33.80 kPa 387.02 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 36.62 kPa 389.45 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 40.00 kPa 391.78 Vapor Liquid Equilibria Measurements for the Nine n-Alkane/Ketone Pairs Comprising 2-, 3-, and 4-Heptanone with n-Octane, n-Nonane, and n-Decane
Pvap 39.52 kPa 391.80 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 40.00 kPa 391.87 Vapor Liquid Equilibria Measurements for the Nine n-Alkane/Ketone Pairs Comprising 2-, 3-, and 4-Heptanone with n-Octane, n-Nonane, and n-Decane
Pvap 40.00 kPa 391.90 Vapor Liquid Equilibria Measurements for the Nine n-Alkane/Ketone Pairs Comprising 2-, 3-, and 4-Heptanone with n-Octane, n-Nonane, and n-Decane
Pvap 40.00 kPa 392.17 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 39.96 kPa 392.77 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 41.74 kPa 393.48 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 44.15 kPa 395.26 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 46.56 kPa 396.96 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 49.15 kPa 398.71 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 49.24 kPa 399.76 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 52.12 kPa 400.61 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 54.42 kPa 402.01 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 56.55 kPa 403.31 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 58.04 kPa 404.65 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 59.01 kPa 404.73 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 61.77 kPa 406.27 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 64.58 kPa 407.78 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 66.76 kPa 408.93 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 66.68 kPa 409.14 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 69.09 kPa 410.11 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 71.53 kPa 411.32 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 74.01 kPa 412.52 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 75.48 kPa 413.23 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 76.48 kPa 413.68 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 79.03 kPa 414.83 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 81.41 kPa 415.90 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 84.18 kPa 417.05 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 84.44 kPa 417.22 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 86.85 kPa 418.24 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 89.41 kPa 419.28 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 92.43 kPa 420.50 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 93.72 kPa 420.83 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 95.25 kPa 421.62 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 98.40 kPa 422.83 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 99.35 kPa 423.20 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 100.44 kPa 423.61 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 101.30 kPa 423.80 Isobaric vapor-liquid equilibrium for the binary mixtures of nonane with cyclohexane, toluene, m-xylene, or p-xylene at 101.3 kPa
Pvap 101.70 kPa 423.88 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 101.32 kPa 423.94 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 104.00 kPa 424.92 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 106.50 kPa 425.83 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 108.99 kPa 426.71 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 111.54 kPa 427.60 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 113.88 kPa 428.40 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 116.44 kPa 429.26 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 119.35 kPa 430.22 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 122.04 kPa 431.09 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 124.99 kPa 432.04 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 127.82 kPa 432.94 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 130.52 kPa 433.74 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 133.60 kPa 434.68 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 136.62 kPa 435.58 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 139.12 kPa 436.31 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 141.90 kPa 437.11 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 144.81 kPa 437.95 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 147.42 kPa 438.67 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 150.23 kPa 439.45 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 152.67 kPa 440.11 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 155.08 kPa 440.76 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 157.53 kPa 441.41 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 159.98 kPa 442.05 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 162.80 kPa 442.77 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 165.61 kPa 443.49 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 168.53 kPa 444.23 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 171.39 kPa 444.93 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 173.63 kPa 445.49 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 176.52 kPa 446.19 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 178.85 kPa 446.75 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 181.82 kPa 447.44 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 184.55 kPa 448.07 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 186.86 kPa 448.61 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 189.75 kPa 449.27 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 192.00 kPa 449.81 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
Pvap 195.54 kPa 450.56 Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
n0 [1.39380; 1.40740]   [293.13; 318.15] Show Hide
n0 1.40550 293.13 Isobaric Vapor-Liquid Equilibria of the Ternary System Pentan-1-ol + Pentyl Acetate + Nonane
n0 1.40580 293.15 Activity Coefficients at Infinite Dilution and Excess Molar Volumes in Binary Mixtures Containing Normal Alkanes (Nonane, Decane, Undecane, or Dodecane) and Cresols (2-Methylphenol or 3-Methylphenol)
n0 1.40400 293.15 Physical properties of {anisole + n-alkanes} at temperatures between (293.15 and 303.15) K
n0 1.40550 293.15 Isobaric Vapor Liquid Equilibria of the Ternary System 1-Pentanol + Nonane Anisole
n0 1.40680 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 1.40550 293.15 Isobaric Vapor-Liquid Equilibria of the Ternary System Dibutyl Ether + 1-Pentanol + Nonane
n0 1.40550 293.15 Activity Coefficients at Infinite Dilution of Cylcohexylamine + Octane, Toluene, Ethylbenzene, or Aniline and Excess Molar Volumes in Binary Mixtures of Cyclohexylamine + Heptane, Octane, Nonane, Decane, Undecane, Aniline, or Water
n0 1.40550 293.15 Isobaric Vapor-Liquid Equilibria of the Ternary System Methylbutyl Ketone + 1-Pentanol + Nonane
n0 1.40740 293.15 Vapor-Liquid Equilibrium Measurements of Ethanol and n-Nonane or n-Decane Binary Mixtures with Large Relative Volatility
n0 1.40560 293.15 P-rho-T Data and Modeling for Propan-1-ol + n-Octane or n-Nonane or n-Decane from 313.15 K to 363.15 K and 1 MPa to 20 MPa
n0 1.40570 293.15 Infinite Dilution Activity Coefficients of Hydrocarbons in Triethylene Glycol and Tetraethylene Glycol
n0 1.40320 298.15 Measurements and Correlations of the Isobaric Vapor Liquid Equilibria of Binary Mixtures and Excess Properties for Mixtures Containing an Alkyl (Methyl, Ethyl) Butanoate with an Alkane (Heptane, Nonane) at 101.3 kPa
n0 1.40310 298.15 Multiproperty Correlation of Experimental Data of the Binaries Propyl Ethanoate + Alkanes (Pentane to Decane). New Experimental Information for Vapor Liquid Equilibrium and Mixing Properties
n0 1.40311 298.15 KDB
n0 1.40270 298.15 Physical properties of {anisole + n-alkanes} at temperatures between (293.15 and 303.15) K
n0 1.40326 298.15 Separation of Benzene from Linear Alkanes (C6-C9) Using 1-Ethyl-3-Methylimidazolium Ethylsulfate at T = 298.15 K
n0 1.40326 298.15 Liquid-Liquid Equilibria of the Ternary Systems of Alkane + Aromatic + 1-Ethylpyridinium Ethylsulfate Ionic Liquid at T = (283.15 and 298.15) K
n0 1.40210 298.15 Excess properties of the binary mixtures of methylcyclohexane + alkanes (C6 to C12) at T = 298.15 K to T = 308.15 K
n0 1.40320 298.15 Improvements in the Experimentation and the Representation of Thermodynamic Properties (iso-p VLE and yE) of Alkyl Propanoate + Alkane Binaries
n0 1.40326 298.15 Extraction of toluene from aliphatic compounds using an ionic liquid as solvent: Influence of the alkane on the (liquid + liquid) equilibrium
n0 1.40220 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 1.40020 303.15 Physical properties of {anisole + n-alkanes} at temperatures between (293.15 and 303.15) K
n0 1.39980 303.15 Excess properties of the binary mixtures of methylcyclohexane + alkanes (C6 to C12) at T = 298.15 K to T = 308.15 K
n0 1.39730 308.15 Excess properties of the binary mixtures of methylcyclohexane + alkanes (C6 to C12) at T = 298.15 K to T = 308.15 K
n0 1.39380 318.15 Multiproperty Correlation of Experimental Data of the Binaries Propyl Ethanoate + Alkanes (Pentane to Decane). New Experimental Information for Vapor Liquid Equilibrium and Mixing Properties
n0 1.39390 318.15 Thermodynamic properties of (an ester + an alkane). XVI. Experimental HEm and V Em values and a new correlation method for (an alkyl ethanoate + an n-alkane) at 318.15 K
ρl [661.14; 732.83] kg/m3 [273.15; 363.15] Show Hide
ρl 732.83 kg/m3 273.15 Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl 729.01 kg/m3 278.15 Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl 725.58 kg/m3 283.15 Density, viscosity and excess molar volume of binary mixtures of tri-n-octylamine + diluents (n-heptane, n-octane, n-nonane, and n-decane) at various temperatures
ρl 725.16 kg/m3 283.15 Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl 724.54 kg/m3 285.15 Measurements of Density and Heat Capacity for Binary Mixtures {x Benzonitrile + (1 -x) (Octane or Nonane)}
ρl 721.32 kg/m3 288.15 Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl 722.22 kg/m3 288.15 Measurements of Density and Heat Capacity for Binary Mixtures {x Benzonitrile + (1 -x) (Octane or Nonane)}
ρl 721.64 kg/m3 288.15 Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl 721.77 kg/m3 288.15 On the permittivity and density measurements of binary systems of {triglyme + (n-nonane or n-dodecane) } at various temperatures
ρl 718.00 kg/m3 293.00 KDB
ρl 717.86 kg/m3 293.15 Density, viscosity and excess molar volume of binary mixtures of tri-n-octylamine + diluents (n-heptane, n-octane, n-nonane, and n-decane) at various temperatures
ρl 718.00 kg/m3 293.15 Volume expansion prediction of supercritical CO 2 + crude oil
ρl 718.42 kg/m3 293.15 Liquid liquid equilibrium of ternary systems 1-butyl-3-methylimidazolium hexafluorophosphate + aromatic + aliphatic
ρl 718.35 kg/m3 293.15 Measurements of Density and Heat Capacity for Binary Mixtures {x Benzonitrile + (1 -x) (Octane or Nonane)}
ρl 717.88 kg/m3 293.15 An Isothermal vapour-liquid equilibrium data for the binary systems of CHF3 with (n-nonane, n-decane, or n-undecane) and C2F6 with (n-nonane or n-decane)
ρl 717.88 kg/m3 293.15 Excess Molar Volumes and Viscosities of Binary Systems of Butylcyclohexane with n-Alkanes (C7 to C14) at T = 293.15 K to 313.15 K
ρl 717.45 kg/m3 293.15 Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl 717.94 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 717.76 kg/m3 293.15 On the permittivity and density measurements of binary systems of {triglyme + (n-nonane or n-dodecane) } at various temperatures
ρl 717.78 kg/m3 293.15 Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl 716.60 kg/m3 294.15 An Isothermal vapour-liquid equilibrium data for the binary systems of CHF3 with (n-nonane, n-decane, or n-undecane) and C2F6 with (n-nonane or n-decane)
ρl 715.82 kg/m3 295.15 An Isothermal vapour-liquid equilibrium data for the binary systems of CHF3 with (n-nonane, n-decane, or n-undecane) and C2F6 with (n-nonane or n-decane)
ρl 715.04 kg/m3 296.15 An Isothermal vapour-liquid equilibrium data for the binary systems of CHF3 with (n-nonane, n-decane, or n-undecane) and C2F6 with (n-nonane or n-decane)
ρl 714.27 kg/m3 297.15 An Isothermal vapour-liquid equilibrium data for the binary systems of CHF3 with (n-nonane, n-decane, or n-undecane) and C2F6 with (n-nonane or n-decane)
ρl 713.69 kg/m3 298.15 An Isothermal vapour-liquid equilibrium data for the binary systems of CHF3 with (n-nonane, n-decane, or n-undecane) and C2F6 with (n-nonane or n-decane)
ρl 714.00 kg/m3 298.15 Excess Molar Volumes and Viscosities of Binary Systems of Butylcyclohexane with n-Alkanes (C7 to C14) at T = 293.15 K to 313.15 K
ρl 714.06 kg/m3 298.15 Thermodynamics of mixtures containing amines VI. Liquid liquid equilibria for mixtures of o-toluidine + selected alkanes
ρl 713.91 kg/m3 298.15 Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl 713.77 kg/m3 298.15 On the permittivity and density measurements of binary systems of {triglyme + (n-nonane or n-dodecane) } at various temperatures
ρl 713.99 kg/m3 298.15 Evaluation of ionic liquids as solvent for aromatic extraction: Experimental, correlation and COSMO-RS predictions
ρl 713.58 kg/m3 298.15 Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl 714.01 kg/m3 298.15 Excess molar volumes and dynamic viscosities for binary mixtures of toluene + n-alkanes (C5 C10) at T = 298.15 K Comparison with Prigogine Flory Patterson theory
ρl 714.46 kg/m3 298.15 Measurements of Density and Heat Capacity for Binary Mixtures {x Benzonitrile + (1 -x) (Octane or Nonane)}
ρl 714.11 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 714.05 kg/m3 298.15 Liquid-liquid equilibria for (2-hydroxy benzaldehyde + n-alkane) mixtures. Intermolecular and proximity effects in systems containing hydroxyl and aldehyde groups
ρl 714.00 kg/m3 298.15 Excess molar enthalpies for binary mixtures of cyclopentanone, cyclohexanone, or cycloheptanone with n-nonane at T = 298.15 K and atmospheric pressure
ρl 714.06 kg/m3 298.15 Thermodynamics of Mixtures Containing a Strongly Polar Compound. 9. Liquid-Liquid Equilibria for epsilon-Caprolactam + Selected Alkanes
ρl 714.06 kg/m3 298.15 Thermodynamics of Mixtures Containing a Strongly Polar Compound. 8. Liquid-Liquid Equilibria for N,N-Dialkylamide + Selected N-Alkanes
ρl 713.90 kg/m3 298.15 (Liquid + liquid) equilibrium at T = 298.15 K for ternary mixtures of alkane + aromatic compounds + imidazolium-based ionic liquids
ρl 713.95 kg/m3 298.15 Density, viscosity and excess molar volume of binary mixtures of tri-n-octylamine + diluents (n-heptane, n-octane, n-nonane, and n-decane) at various temperatures
ρl 713.94 kg/m3 298.20 Apparent and Partial Molar Volumes at Infinite Dilution and Solid Liquid Equilibria of Dibenzothiophene + Alkane Systems
ρl 710.03 kg/m3 303.15 Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl 709.89 kg/m3 303.15 On the permittivity and density measurements of binary systems of {triglyme + (n-nonane or n-dodecane) } at various temperatures
ρl 710.10 kg/m3 303.15 Excess Molar Volumes and Viscosities of Binary Systems of Butylcyclohexane with n-Alkanes (C7 to C14) at T = 293.15 K to 313.15 K
ρl 710.55 kg/m3 303.15 Measurements of Density and Heat Capacity for Binary Mixtures {x Benzonitrile + (1 -x) (Octane or Nonane)}
ρl 710.20 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 710.06 kg/m3 303.15 Density, viscosity and excess molar volume of binary mixtures of tri-n-octylamine + diluents (n-heptane, n-octane, n-nonane, and n-decane) at various temperatures
ρl 709.69 kg/m3 303.15 Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl 706.12 kg/m3 308.15 Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl 706.63 kg/m3 308.15 Measurements of Density and Heat Capacity for Binary Mixtures {x Benzonitrile + (1 -x) (Octane or Nonane)}
ρl 706.20 kg/m3 308.15 On the permittivity and density measurements of binary systems of {triglyme + (n-nonane or n-dodecane) } at various temperatures
ρl 706.19 kg/m3 308.15 Excess Molar Volumes and Viscosities of Binary Systems of Butylcyclohexane with n-Alkanes (C7 to C14) at T = 293.15 K to 313.15 K
ρl 706.29 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 705.78 kg/m3 308.15 Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl 702.35 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 701.86 kg/m3 313.15 Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl 702.70 kg/m3 313.15 Measurements of Density and Heat Capacity for Binary Mixtures {x Benzonitrile + (1 -x) (Octane or Nonane)}
ρl 702.26 kg/m3 313.15 Excess Molar Volumes and Viscosities of Binary Systems of Butylcyclohexane with n-Alkanes (C7 to C14) at T = 293.15 K to 313.15 K
ρl 702.20 kg/m3 313.15 Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl 698.14 kg/m3 318.15 On the permittivity and density measurements of binary systems of {triglyme + (n-nonane or n-dodecane) } at various temperatures
ρl 698.26 kg/m3 318.15 Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl 697.91 kg/m3 318.15 Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl 698.40 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 693.95 kg/m3 323.15 Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl 694.43 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 694.30 kg/m3 323.15 Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl 690.14 kg/m3 328.15 On the permittivity and density measurements of binary systems of {triglyme + (n-nonane or n-dodecane) } at various temperatures
ρl 690.33 kg/m3 328.15 Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl 689.97 kg/m3 328.15 Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl 685.97 kg/m3 333.15 Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl 686.34 kg/m3 333.15 Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl 681.94 kg/m3 338.15 Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl 682.31 kg/m3 338.15 Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl 677.88 kg/m3 343.15 Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl 678.26 kg/m3 343.15 Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
ρl 673.91 kg/m3 348.15 Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl 669.71 kg/m3 353.15 Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl 665.58 kg/m3 358.15 Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
ρl 661.14 kg/m3 363.15 Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
csound,fluid [738.00; 1227.30] m/s [293.15; 423.15] Show Hide
csound,fluid 1227.30 m/s 293.15 Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid 1207.20 m/s 298.15 Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid 1187.20 m/s 303.15 Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid 1167.30 m/s 308.15 Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid 1147.50 m/s 313.15 Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid 1127.80 m/s 318.15 Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid 1108.20 m/s 323.15 Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid 1088.70 m/s 328.15 Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid 1069.30 m/s 333.15 Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid 1050.00 m/s 338.15 Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid 1030.80 m/s 343.15 Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid 1011.80 m/s 348.15 Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid 992.80 m/s 353.15 Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid 973.90 m/s 358.15 Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid 955.20 m/s 363.15 Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid 936.50 m/s 368.15 Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid 917.90 m/s 373.15 Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid 899.50 m/s 378.15 Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid 881.10 m/s 383.15 Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid 862.90 m/s 388.15 Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid 844.70 m/s 393.15 Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid 826.70 m/s 398.15 Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid 808.80 m/s 403.15 Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid 790.90 m/s 408.15 Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid 773.20 m/s 413.15 Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid 755.60 m/s 418.15 Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
csound,fluid 738.00 m/s 423.15 Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
γ [0.02; 0.02] N/m [288.15; 323.15] Show Hide
γ 0.02 N/m 288.15 Density and surface tension variation with temperature for n-nonane + 1-hexanol
γ 0.02 N/m 293.15 Density, Refractive Index, Viscosity, and Surface Tension of Binary Mixtures of exo-Tetrahydrodicyclopentadiene with Some n-Alkanes from (293.15 to 313.15) K
γ 0.02 N/m 293.15 Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
γ 0.02 N/m 293.15 Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
γ 0.02 N/m 293.20 KDB
γ 0.02 N/m 298.15 Density and surface tension variation with temperature for n-nonane + 1-hexanol
γ 0.02 N/m 298.15 Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
γ 0.02 N/m 298.15 Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
γ 0.02 N/m 303.15 Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
γ 0.02 N/m 303.15 Density, Refractive Index, Viscosity, and Surface Tension of Binary Mixtures of exo-Tetrahydrodicyclopentadiene with Some n-Alkanes from (293.15 to 313.15) K
γ 0.02 N/m 303.15 Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
γ 0.02 N/m 308.15 Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
γ 0.02 N/m 308.15 Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
γ 0.02 N/m 308.15 Density and surface tension variation with temperature for n-nonane + 1-hexanol
γ 0.02 N/m 313.15 Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
γ 0.02 N/m 313.15 Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
γ 0.02 N/m 318.15 Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
γ 0.02 N/m 318.15 Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
γ 0.02 N/m 323.15 Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
γ 0.02 N/m 323.15 Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures

Datasets

  1. Isobaric coefficient of expansion, 1/K (1)
  2. Viscosity, Pa*s (1)
  3. Mass density, kg/m3 (5)
  4. Speed of sound, m/s (1)

Isobaric coefficient of expansion, 1/K

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Isobaric coefficient of expansion, 1/K - Liquid
278.15 5000.00 0.0010
278.15 10000.00 0.0010
278.15 15000.00 0.0010
278.15 20000.00 0.0009
278.15 25000.00 0.0009
278.15 30000.00 0.0009
278.15 35000.00 0.0009
278.15 40000.00 0.0008
278.15 45000.00 0.0008
278.15 50000.00 0.0008
278.15 55000.00 0.0008
288.15 5000.00 0.0010
288.15 10000.00 0.0010
288.15 15000.00 0.0010
288.15 20000.00 0.0009
288.15 25000.00 0.0009
288.15 30000.00 0.0009
288.15 35000.00 0.0009
288.15 40000.00 0.0009
288.15 45000.00 0.0008
288.15 50000.00 0.0008
288.15 55000.00 0.0008
298.15 5000.00 0.0010
298.15 10000.00 0.0010
298.15 15000.00 0.0010
298.15 20000.00 0.0010
298.15 25000.00 0.0009
298.15 30000.00 0.0009
298.15 35000.00 0.0009
298.15 40000.00 0.0009
298.15 45000.00 0.0008
298.15 50000.00 0.0008
298.15 55000.00 0.0008
308.15 5000.00 0.0011
308.15 10000.00 0.0010
308.15 15000.00 0.0010
308.15 20000.00 0.0010
308.15 25000.00 0.0009
308.15 30000.00 0.0009
308.15 35000.00 0.0009
308.15 40000.00 0.0009
308.15 45000.00 0.0008
308.15 50000.00 0.0008
308.15 55000.00 0.0008
318.15 5000.00 0.0011
318.15 10000.00 0.0010
318.15 15000.00 0.0010
318.15 20000.00 0.0010
318.15 25000.00 0.0009
318.15 30000.00 0.0009
318.15 35000.00 0.0009
318.15 40000.00 0.0009
318.15 45000.00 0.0008
318.15 50000.00 0.0008
318.15 55000.00 0.0008
328.15 5000.00 0.0011
328.15 10000.00 0.0011
328.15 15000.00 0.0010
328.15 20000.00 0.0010
328.15 25000.00 0.0009
328.15 30000.00 0.0009
328.15 35000.00 0.0009
328.15 40000.00 0.0009
328.15 45000.00 0.0008
328.15 50000.00 0.0008
328.15 55000.00 0.0008
338.15 5000.00 0.0011
338.15 10000.00 0.0011
338.15 15000.00 0.0010
338.15 20000.00 0.0010
338.15 25000.00 0.0010
338.15 30000.00 0.0009
338.15 35000.00 0.0009
338.15 40000.00 0.0009
338.15 45000.00 0.0008
338.15 50000.00 0.0008
338.15 55000.00 0.0008
348.15 5000.00 0.0011
348.15 10000.00 0.0011
348.15 15000.00 0.0010
348.15 20000.00 0.0010
348.15 25000.00 0.0010
348.15 30000.00 0.0009
348.15 35000.00 0.0009
348.15 40000.00 0.0009
348.15 45000.00 0.0008
348.15 50000.00 0.0008
348.15 55000.00 0.0008
Reference

Viscosity, Pa*s

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Viscosity, Pa*s - Liquid
303.15 101.33 0.0006
Reference

Mass density, kg/m3

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
233.15 101.46 763.962
233.15 1176.07 764.563
233.15 2178.21 765.126
233.15 4167.03 766.231
233.15 5936.52 767.203
233.15 8144.53 768.395
233.15 10065.60 769.42
233.15 12147.70 770.516
233.15 14076.40 771.516
233.15 16087.10 772.548
233.15 18066.90 773.551
233.15 19984.50 774.511
233.15 21989.60 775.502
233.15 24043.80 776.506
233.15 25990.20 777.446
233.15 27926.70 778.373
233.15 29906.00 779.308
253.15 101.82 748.678
253.15 1135.27 749.335
253.15 2178.61 749.992
253.15 3967.76 751.107
253.15 6147.47 752.446
253.15 8137.98 753.648
253.15 10112.30 754.82
253.15 12111.20 755.991
253.15 14130.20 757.156
253.15 16140.10 758.299
253.15 18106.10 759.398
253.15 20064.20 760.484
253.15 22026.10 761.552
253.15 23955.00 762.59
253.15 25972.30 763.661
253.15 27912.60 764.677
253.15 29966.80 765.739
273.15 102.52 733.389
273.15 1156.84 734.143
273.15 2137.97 734.842
273.15 4026.01 736.166
273.15 6169.44 737.644
273.15 8161.45 738.99
273.15 10122.00 740.29
273.15 12106.50 741.586
273.15 14100.70 742.864
273.15 16067.00 744.108
273.15 18074.30 745.354
273.15 20036.30 746.555
273.15 21999.70 747.737
273.15 23995.50 748.923
273.15 25993.50 750.093
273.15 27981.50 751.238
273.15 29875.50 752.316
293.15 101.69 717.968
293.15 1184.28 718.847
293.15 2129.17 719.604
293.15 3960.49 721.055
293.15 6115.45 722.729
293.15 7981.56 724.145
293.15 10014.70 725.663
293.15 12148.60 727.214
293.15 13981.10 728.526
293.15 16170.10 730.062
293.15 17942.90 731.285
293.15 20200.00 732.813
293.15 22156.50 734.115
293.15 24157.90 735.421
293.15 26136.50 736.696
293.15 28126.30 737.958
293.15 29978.50 739.115
313.15 98.73 702.339
313.15 1168.73 703.323
313.15 2131.95 704.205
313.15 3967.37 705.852
313.15 6162.29 707.777
313.15 8113.86 709.449
313.15 10023.50 711.038
313.15 12172.80 712.791
313.15 14170.00 714.384
313.15 16194.40 715.964
313.15 17956.10 717.315
313.15 20057.40 718.889
313.15 22190.80 720.459
313.15 24136.30 721.862
313.15 26139.10 723.282
313.15 28073.10 724.629
313.15 29972.40 725.932
333.15 102.84 686.431
333.15 1137.45 687.521
333.15 2113.93 688.539
333.15 4162.71 690.632
333.15 6145.33 692.599
333.15 8151.89 694.535
333.15 10023.60 696.296
333.15 12113.90 698.208
333.15 14126.60 700.005
333.15 15989.20 701.627
333.15 18027.40 703.362
333.15 19954.20 704.977
333.15 22112.40 706.723
333.15 24079.90 708.292
333.15 26037.60 709.821
333.15 28054.20 711.366
333.15 29912.30 712.772
353.15 97.13 671.217
353.15 2136.70 672.617
353.15 6141.90 677.222
353.15 8110.87 679.378
353.15 10054.10 681.439
353.15 12124.00 683.57
353.15 14143.80 685.589
353.15 15989.00 687.385
353.15 18010.60 689.305
353.15 20035.80 691.174
353.15 21991.10 692.938
353.15 23964.80 694.678
353.15 25968.30 696.403
353.15 27955.30 698.078
353.15 29938.70 699.718
373.15 102.37 653.427
373.15 1227.94 655.018
373.15 2148.86 656.298
373.15 4131.53 658.968
373.15 6127.03 661.551
373.15 8138.76 664.058
373.15 10022.20 666.323
373.15 12111.60 668.749
373.15 14118.80 671.003
373.15 16133.90 673.197
373.15 18104.00 675.276
373.15 20078.30 677.302
373.15 22063.50 679.286
373.15 23987.70 681.158
373.15 26124.00 683.184
373.15 28010.20 684.93
373.15 29904.70 686.647
Reference
Fixed Measured
Pressure, kPa - Liquid Temperature, K - Liquid Mass density, kg/m3 - Liquid
100.00 298.15 713.93
Reference
Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
283.15 1010.00 726.22
283.15 5040.00 729.17
283.15 10020.00 732.75
283.15 15020.00 736.14
283.15 20040.00 739.41
283.15 25020.00 742.54
283.15 30040.00 745.52
283.15 35050.00 748.45
283.15 40010.00 751.23
283.15 45050.00 753.99
283.15 50010.00 756.62
283.15 55020.00 759.19
283.15 60030.00 761.66
283.15 65010.00 764.08
283.15 5020.00 729.22
298.15 1020.00 714.83
298.15 5010.00 718.08
298.15 10030.00 721.94
298.15 15060.00 725.7
298.15 20040.00 729.17
298.15 25040.00 732.54
298.15 30010.00 735.76
298.15 35050.00 738.87
298.15 40010.00 741.88
298.15 45060.00 744.79
298.15 50010.00 747.56
298.15 55040.00 750.31
298.15 60020.00 752.92
298.15 65010.00 755.48
298.15 5040.00 718.12
323.15 1030.00 695.27
323.15 5030.00 699.04
323.15 10050.00 703.57
323.15 15020.00 707.81
323.15 20050.00 711.84
323.15 25020.00 715.63
323.15 30020.00 719.22
323.15 35080.00 722.75
323.15 40050.00 726.09
323.15 45060.00 729.27
323.15 50030.00 732.36
323.15 55050.00 735.35
323.15 60010.00 738.19
323.15 65010.00 741.02
323.15 5060.00 699.09
348.15 1010.00 675.18
348.15 5040.00 679.76
348.15 10030.00 685.0
348.15 15020.00 689.84
348.15 20040.00 694.44
348.15 25050.00 698.79
348.15 30030.00 702.84
348.15 35050.00 706.74
348.15 40020.00 710.4
348.15 45070.00 714.01
348.15 50040.00 717.37
348.15 55050.00 720.67
348.15 60000.00 723.79
348.15 65040.00 726.84
348.15 5030.00 679.76
373.15 1010.00 654.52
373.15 5050.00 659.99
373.15 10030.00 666.13
373.15 15070.00 671.78
373.15 20030.00 677.04
373.15 25060.00 681.94
373.15 30040.00 686.51
373.15 35060.00 690.83
373.15 40020.00 694.95
373.15 45070.00 698.87
373.15 50070.00 702.65
373.15 55060.00 706.23
373.15 60040.00 709.66
373.15 65030.00 712.95
373.15 5050.00 659.99
398.15 1020.00 633.06
398.15 5020.00 639.53
398.15 10050.00 646.89
398.15 15070.00 653.53
398.15 20020.00 659.49
398.15 25030.00 665.05
398.15 30050.00 670.22
398.15 35050.00 675.1
398.15 40020.00 679.63
398.15 45070.00 683.97
398.15 50020.00 688.07
398.15 55040.00 692.01
398.15 60030.00 695.72
398.15 65040.00 699.37
398.15 5030.00 639.58
423.15 1020.00 610.45
423.15 5030.00 618.42
423.15 10030.00 627.15
423.15 15030.00 634.86
423.15 20040.00 641.8
423.15 25040.00 648.1
423.15 30020.00 653.92
423.15 35050.00 659.35
423.15 40020.00 664.4
423.15 45020.00 669.15
423.15 50040.00 673.7
423.15 55020.00 677.97
423.15 60030.00 682.03
423.15 65040.00 685.95
423.15 5030.00 618.47
448.15 1000.00 586.37
448.15 5020.00 596.41
448.15 10040.00 607.05
448.15 15010.00 616.06
448.15 20010.00 624.0
448.15 25040.00 631.27
448.15 30030.00 637.78
448.15 35030.00 643.8
448.15 40010.00 649.38
448.15 45050.00 654.67
448.15 50020.00 659.58
448.15 55040.00 664.24
448.15 60030.00 668.62
448.15 65020.00 672.85
448.15 5020.00 596.46
473.15 5010.00 573.14
473.15 10040.00 586.15
473.15 15040.00 596.86
473.15 20020.00 606.05
473.15 25050.00 614.28
473.15 30020.00 621.6
473.15 35030.00 628.3
473.15 40050.00 634.51
473.15 45050.00 640.25
473.15 50040.00 645.6
473.15 55020.00 650.62
473.15 60010.00 655.39
473.15 65010.00 659.92
473.15 5010.00 573.14
Reference
Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
293.21 1993.00 719.36
293.21 3991.00 721.16
293.21 5993.00 722.88
293.21 7996.00 724.42
293.21 10001.00 725.92
293.21 13001.00 728.0
293.22 16000.00 730.02
293.21 19004.00 732.11
293.21 22005.00 734.14
293.21 24997.00 736.13
293.21 27997.00 738.31
293.21 29995.00 739.58
313.11 2000.00 704.08
313.11 4007.00 705.88
313.11 6006.00 707.62
313.11 8004.00 709.24
313.11 10007.00 710.92
313.11 13003.00 713.28
313.11 16007.00 715.76
313.10 19007.00 718.18
313.10 22007.00 720.52
313.10 25009.00 722.7
313.10 28007.00 724.82
313.10 30010.00 726.21
333.00 2014.00 688.53
333.00 3990.00 690.6
333.00 5995.00 692.58
333.01 8001.00 694.51
333.01 10007.00 696.11
333.01 13004.00 698.84
333.01 16002.00 701.48
333.01 19006.00 704.03
333.01 22003.00 706.5
333.01 25006.00 708.9
333.01 28003.00 711.23
333.01 30012.00 712.74
353.12 2004.00 672.27
353.12 3995.00 674.59
353.12 6000.00 676.83
353.12 8005.00 679.1
353.12 10010.00 681.31
353.12 13002.00 684.37
353.12 16003.00 687.3
353.12 18999.00 689.99
353.12 22002.00 692.72
353.12 25004.00 695.35
353.12 28007.00 697.9
353.12 30003.00 699.56
Reference
Fixed Measured
Pressure, kPa - Liquid Temperature, K - Liquid Mass density, kg/m3 - Liquid
100.00 283.15 725.6
100.00 288.15 721.6
100.00 293.15 717.8
100.00 298.15 713.7
100.00 303.15 709.9
100.00 308.15 706.0
100.00 313.15 701.9
100.00 318.15 698.1
100.00 323.15 694.1
3000.00 283.15 727.7
3000.00 288.15 723.8
3000.00 293.15 720.0
3000.00 298.15 716.1
3000.00 303.15 712.3
3000.00 308.15 708.5
3000.00 313.15 704.5
3000.00 318.15 700.7
3000.00 323.15 696.9
5000.00 283.15 729.1
5000.00 288.15 725.3
5000.00 293.15 721.5
5000.00 298.15 717.7
5000.00 303.15 713.9
5000.00 308.15 710.1
5000.00 313.15 706.3
5000.00 318.15 702.4
5000.00 323.15 698.6
7500.00 283.15 730.8
7500.00 288.15 727.0
7500.00 293.15 723.4
7500.00 298.15 719.5
7500.00 303.15 715.8
7500.00 308.15 712.1
7500.00 313.15 708.3
7500.00 318.15 704.6
7500.00 323.15 700.8
10000.00 283.15 732.6
10000.00 288.15 728.9
10000.00 293.15 725.2
10000.00 298.15 721.5
10000.00 303.15 717.8
10000.00 308.15 714.2
10000.00 313.15 710.4
10000.00 318.15 706.8
10000.00 323.15 703.0
20000.00 283.15 739.2
20000.00 288.15 735.7
20000.00 293.15 732.2
20000.00 298.15 728.7
20000.00 303.15 725.2
20000.00 308.15 721.7
20000.00 313.15 718.2
20000.00 318.15 714.7
20000.00 323.15 711.2
30000.00 283.15 745.3
30000.00 288.15 742.0
30000.00 293.15 738.7
30000.00 298.15 735.2
30000.00 303.15 731.9
30000.00 308.15 728.5
30000.00 313.15 725.3
30000.00 318.15 721.9
30000.00 323.15 718.6
40000.00 283.15 751.1
40000.00 288.15 747.9
40000.00 293.15 744.6
40000.00 298.15 741.4
40000.00 303.15 738.2
40000.00 308.15 735.0
40000.00 313.15 731.8
40000.00 318.15 728.6
40000.00 323.15 725.4
50000.00 283.15 756.4
50000.00 288.15 753.4
50000.00 293.15 750.3
50000.00 298.15 747.1
50000.00 303.15 744.1
50000.00 308.15 740.9
50000.00 313.15 737.8
50000.00 318.15 734.8
50000.00 323.15 731.6
60000.00 283.15 761.6
60000.00 288.15 758.5
60000.00 293.15 755.5
60000.00 298.15 752.5
60000.00 303.15 749.5
60000.00 308.15 746.6
60000.00 313.15 743.5
60000.00 318.15 740.5
60000.00 323.15 737.5
Reference

Speed of sound, m/s

Fixed Measured
Pressure, kPa - Liquid Temperature, K - Liquid Speed of sound, m/s - Liquid
100.00 293.15 1226.379
100.00 313.15 1146.226
100.00 333.15 1068.198
100.00 353.15 992.6189
100.00 373.15 922.1599
100.00 393.15 867.4314
10000.00 293.15 1288.02
10000.00 313.15 1212.824
10000.00 333.15 1140.94
10000.00 353.15 1072.568
10000.00 373.15 1004.987
10000.00 393.15 946.865
20000.00 293.15 1344.821
20000.00 313.15 1274.241
20000.00 333.15 1206.915
20000.00 353.15 1142.609
20000.00 373.15 1081.282
20000.00 393.15 1022.924
30000.00 293.15 1396.854
30000.00 313.15 1329.834
30000.00 333.15 1266.203
30000.00 353.15 1205.597
30000.00 373.15 1148.091
30000.00 393.15 1093.674
40000.00 293.15 1445.084
40000.00 313.15 1380.943
40000.00 353.15 1262.461
40000.00 373.15 1207.979
40000.00 393.15 1156.595
50000.00 293.15 1490.057
50000.00 313.15 1428.288
50000.00 333.15 1369.835
50000.00 353.15 1314.591
50000.00 373.15 1262.528
50000.00 393.15 1213.59
60000.00 293.15 1532.464
60000.00 313.15 1472.742
60000.00 333.15 1416.313
60000.00 353.15 1363.169
60000.00 373.15 1313.133
60000.00 393.15 1266.136
70000.00 293.15 1572.512
70000.00 313.15 1514.719
70000.00 333.15 1460.059
70000.00 353.15 1408.501
70000.00 373.15 1360.053
70000.00 393.15 1314.71
80000.00 293.15 1610.591
80000.00 313.15 1554.351
80000.00 333.15 1501.308
80000.00 353.15 1451.316
80000.00 373.15 1404.349
80000.00 393.15 1360.387
90000.00 293.15 1646.928
90000.00 313.15 1592.049
90000.00 333.15 1540.349
90000.00 353.15 1491.697
90000.00 373.15 1446.071
90000.00 393.15 1403.307
100000.00 293.15 1681.563
100000.00 313.15 1628.026
100000.00 333.15 1577.369
100000.00 353.15 1529.841
100000.00 373.15 1485.463
100000.00 393.15 1443.653
Reference

Correlations

Property Value Unit Temperature (K) Source
Cp,gas [161.43; 554.96] J/mol×K [200.00; 1500.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is Cp,gas in J/mol×K, T in K
Coefficient A1.37710e+02
Coefficient B-6.99520e+02
Coefficient C6.70524e+00
Coefficient D-2.17350e-04
Coefficient E5.36950e-08
Temperature range, min.200.00
Temperature range, max.1500.00
Cp,gas 161.43 J/mol×K 200.00 Calculated Property
Cp,gas 237.78 J/mol×K 344.44 Calculated Property
Cp,gas 315.57 J/mol×K 488.89 Calculated Property
Cp,gas 378.67 J/mol×K 633.33 Calculated Property
Cp,gas 427.54 J/mol×K 777.78 Calculated Property
Cp,gas 465.36 J/mol×K 922.22 Calculated Property
Cp,gas 495.05 J/mol×K 1066.67 Calculated Property
Cp,gas 518.86 J/mol×K 1211.11 Calculated Property
Cp,gas 538.42 J/mol×K 1355.56 Calculated Property
Cp,gas 554.96 J/mol×K 1500.00 Calculated Property
Property Value Unit Temperature (K) Source
Cp,liquid [263.72; 298.74] J/mol×K [219.66; 325.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is Cp,liquid in J/mol×K, T in K
Coefficient A2.63370e+02
Coefficient B-1.44660e+04
Coefficient C1.27132e+02
Coefficient D-3.68230e-01
Coefficient E3.84560e-04
Temperature range, min.219.66
Temperature range, max.325.00
Cp,liquid 263.72 J/mol×K 219.66 Calculated Property
Cp,liquid 264.37 J/mol×K 231.36 Calculated Property
Cp,liquid 265.67 J/mol×K 243.07 Calculated Property
Cp,liquid 267.85 J/mol×K 254.77 Calculated Property
Cp,liquid 270.98 J/mol×K 266.48 Calculated Property
Cp,liquid 275.01 J/mol×K 278.18 Calculated Property
Cp,liquid 279.84 J/mol×K 289.89 Calculated Property
Cp,liquid 285.35 J/mol×K 301.59 Calculated Property
Cp,liquid 291.59 J/mol×K 313.30 Calculated Property
Cp,liquid 298.74 J/mol×K 325.00 Calculated Property
Property Value Unit Temperature (K) Source
η [0.0034265; 0.0000493] Pa×s [218.15; 593.15] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = exp(A + B/T + C·ln(T) + D·T^E)
Y is η in Pa×s, T in K
Coefficient A-7.54880e+01
Coefficient B3.42070e+03
Coefficient C1.01830e+01
Coefficient D-1.48360e-05
Coefficient E2.00000e+00
Temperature range, min.218.15
Temperature range, max.593.15
η 0.0034265 Pa×s 218.15 Calculated Property
η 0.0012230 Pa×s 259.82 Calculated Property
η 0.0006372 Pa×s 301.48 Calculated Property
η 0.0004031 Pa×s 343.15 Calculated Property
η 0.0002805 Pa×s 384.82 Calculated Property
η 0.0002031 Pa×s 426.48 Calculated Property
η 0.0001478 Pa×s 468.15 Calculated Property
η 0.0001059 Pa×s 509.82 Calculated Property
η 0.0000737 Pa×s 551.48 Calculated Property
η 0.0000493 Pa×s 593.15 Calculated Property
Property Value Unit Temperature (K) Source
ΔvapH [52.93; 0.00] kJ/mol [219.63; 594.60] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc
Y is ΔvapH in kJ/mol, T in K
Coefficient A8.42748e+01
Coefficient B1.57375e+00
Coefficient C-1.78592e+00
Coefficient D6.92082e-01
Coefficient E2.68541e-03
Critical temperature, Tc (K)5.94600e+02
Temperature range, min.219.63
Temperature range, max.594.60
ΔvapH 52.93 kJ/mol 219.63 Calculated Property
ΔvapH 49.40 kJ/mol 261.29 Calculated Property
ΔvapH 46.20 kJ/mol 302.96 Calculated Property
ΔvapH 43.18 kJ/mol 344.62 Calculated Property
ΔvapH 40.17 kJ/mol 386.28 Calculated Property
ΔvapH 36.97 kJ/mol 427.95 Calculated Property
ΔvapH 33.25 kJ/mol 469.61 Calculated Property
ΔvapH 28.51 kJ/mol 511.27 Calculated Property
ΔvapH 21.51 kJ/mol 552.94 Calculated Property
ΔvapH 0.00 kJ/mol 594.60 Calculated Property
Property Value Unit Temperature (K) Source
Pvap [1.33; 202.64] kPa [310.51; 451.94] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.45385e+01
Coefficient B-3.70195e+03
Coefficient C-5.07360e+01
Temperature range, min.310.51
Temperature range, max.451.94
Pvap 1.33 kPa 310.51 Calculated Property
Pvap 3.01 kPa 326.22 Calculated Property
Pvap 6.21 kPa 341.94 Calculated Property
Pvap 11.90 kPa 357.65 Calculated Property
Pvap 21.42 kPa 373.37 Calculated Property
Pvap 36.50 kPa 389.08 Calculated Property
Pvap 59.31 kPa 404.80 Calculated Property
Pvap 92.49 kPa 420.51 Calculated Property
Pvap 139.11 kPa 436.23 Calculated Property
Pvap 202.64 kPa 451.94 Calculated Property
Pvap [5.85e-04; 1557.94] kPa [219.66; 594.60] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = exp(A + B/T + C·ln(T) + D·T^E)
Y is Pvap in kPa, T in K
Coefficient A2.74748e+01
Coefficient B-6.23541e+03
Coefficient C-1.15393e+00
Coefficient D-6.40849e-06
Coefficient E2.00000e+00
Temperature range, min.219.66
Temperature range, max.594.60
Pvap 5.85e-04 kPa 219.66 Calculated Property
Pvap 0.04 kPa 261.32 Calculated Property
Pvap 0.75 kPa 302.98 Calculated Property
Pvap 6.55 kPa 344.64 Calculated Property
Pvap 33.23 kPa 386.30 Calculated Property
Pvap 114.35 kPa 427.96 Calculated Property
Pvap 294.40 kPa 469.62 Calculated Property
Pvap 605.99 kPa 511.28 Calculated Property
Pvap 1044.41 kPa 552.94 Calculated Property
Pvap 1557.94 kPa 594.60 Calculated Property
Pvap [6.08e-04; 2266.69] kPa [219.63; 595.65] 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 A7.25466e+01
Coefficient B-7.73941e+03
Coefficient C-8.32740e+00
Coefficient D3.89483e-06
Coefficient E0.00000e+00
Temperature range, min.219.63
Temperature range, max.595.65
Pvap 6.08e-04 kPa 219.63 Calculated Property
Pvap 0.04 kPa 261.41 Calculated Property
Pvap 0.81 kPa 303.19 Calculated Property
Pvap 6.78 kPa 344.97 Calculated Property
Pvap 33.28 kPa 386.75 Calculated Property
Pvap 113.80 kPa 428.53 Calculated Property
Pvap 301.98 kPa 470.31 Calculated Property
Pvap 667.88 kPa 512.09 Calculated Property
Pvap 1292.71 kPa 553.87 Calculated Property
Pvap 2266.69 kPa 595.65 Calculated Property
Pvap [5.14e-04; 0.79] kPa [219.70; 307.73] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.34123e+01
Coefficient B-3.43759e+03
Coefficient C-5.58950e+01
ReferenceCarruth and Kobayashi, 1973
CommentCoefficents calculated by NIST from author's data.
Temperature range, min.219.70
Temperature range, max.307.73
Pvap 5.14e-04 kPa 219.70 Calculated Property
Pvap 1.68e-03 kPa 229.48 Calculated Property
Pvap 4.82e-03 kPa 239.26 Calculated Property
Pvap 0.01 kPa 249.04 Calculated Property
Pvap 0.03 kPa 258.82 Calculated Property
Pvap 0.06 kPa 268.61 Calculated Property
Pvap 0.13 kPa 278.39 Calculated Property
Pvap 0.25 kPa 288.17 Calculated Property
Pvap 0.45 kPa 297.95 Calculated Property
Pvap 0.79 kPa 307.73 Calculated Property
Pvap [6.40; 104.01] kPa [343.49; 424.94] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.39593e+01
Coefficient B-3.29356e+03
Coefficient C-7.13550e+01
ReferenceForziati, Norris, et al., 1949, 2
CommentCoefficents calculated by NIST from author's data.
Temperature range, min.343.49
Temperature range, max.424.94
Pvap 6.40 kPa 343.49 Calculated Property
Pvap 9.45 kPa 352.54 Calculated Property
Pvap 13.62 kPa 361.59 Calculated Property
Pvap 19.19 kPa 370.64 Calculated Property
Pvap 26.51 kPa 379.69 Calculated Property
Pvap 35.95 kPa 388.74 Calculated Property
Pvap 47.93 kPa 397.79 Calculated Property
Pvap 62.93 kPa 406.84 Calculated Property
Pvap 81.44 kPa 415.89 Calculated Property
Pvap 104.01 kPa 424.94 Calculated Property
Pvap [6.40; 104.01] kPa [343.49; 424.94] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.39593e+01
Coefficient B-3.29356e+03
Coefficient C-7.13550e+01
ReferenceForziati, Norris, et al., 1949
CommentCoefficents calculated by NIST from author's data.
Temperature range, min.343.49
Temperature range, max.424.94
Pvap 6.40 kPa 343.49 Calculated Property
Pvap 9.45 kPa 352.54 Calculated Property
Pvap 13.62 kPa 361.59 Calculated Property
Pvap 19.19 kPa 370.64 Calculated Property
Pvap 26.51 kPa 379.69 Calculated Property
Pvap 35.95 kPa 388.74 Calculated Property
Pvap 47.93 kPa 397.79 Calculated Property
Pvap 62.93 kPa 406.84 Calculated Property
Pvap 81.44 kPa 415.89 Calculated Property
Pvap 104.01 kPa 424.94 Calculated Property
Property Value Unit Temperature (K) Source
ρl [771.47; 232.64] kg/m3 [219.66; 594.60] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A / B^(1 + (1 − T/C)^D)
Y is ρl in kg/m3, T in K
Coefficient A5.94834e+01
Coefficient B2.55690e-01
Coefficient C5.94600e+02
Coefficient D2.79610e-01
Temperature range, min.219.66
Temperature range, max.594.60
ρl 771.47 kg/m3 219.66 Calculated Property
ρl 742.08 kg/m3 261.32 Calculated Property
ρl 711.20 kg/m3 302.98 Calculated Property
ρl 678.45 kg/m3 344.64 Calculated Property
ρl 643.30 kg/m3 386.30 Calculated Property
ρl 604.92 kg/m3 427.96 Calculated Property
ρl 561.85 kg/m3 469.62 Calculated Property
ρl 511.18 kg/m3 511.28 Calculated Property
ρl 444.98 kg/m3 552.94 Calculated Property
ρl 232.64 kg/m3 594.60 Calculated Property
Property Value Unit Temperature (K) Source
γ [0.03; 0.01] N/m [219.65; 423.95] 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 A5.02595e-02
Coefficient B-9.35000e-05
Coefficient C0.00000e+00
Coefficient D0.00000e+00
Coefficient E0.00000e+00
Temperature range, min.219.65
Temperature range, max.423.95
γ 0.03 N/m 219.65 Calculated Property
γ 0.03 N/m 242.35 Calculated Property
γ 0.03 N/m 265.05 Calculated Property
γ 0.02 N/m 287.75 Calculated Property
γ 0.02 N/m 310.45 Calculated Property
γ 0.02 N/m 333.15 Calculated Property
γ 0.02 N/m 355.85 Calculated Property
γ 0.01 N/m 378.55 Calculated Property
γ 0.01 N/m 401.25 Calculated Property
γ 0.01 N/m 423.95 Calculated Property
γ [0.03; 1.11e-05] N/m [219.66; 590.85] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is γ in N/m, T in K
Coefficient A-5.69520e-03
Coefficient B1.24020e+02
Coefficient C-4.21390e+00
Coefficient D3.53360e-03
Coefficient E-9.30960e-06
CommentRange stopped where the equation turns negative; ChemSep gives it to 594.6 K.
Temperature range, min.219.66
Temperature range, max.590.85
γ 0.03 N/m 219.66 Calculated Property
γ 0.03 N/m 260.90 Calculated Property
γ 0.02 N/m 302.15 Calculated Property
γ 0.02 N/m 343.39 Calculated Property
γ 0.01 N/m 384.63 Calculated Property
γ 0.01 N/m 425.88 Calculated Property
γ 0.01 N/m 467.12 Calculated Property
γ 0.00 N/m 508.36 Calculated Property
γ 0.00 N/m 549.61 Calculated Property
γ 1.11e-05 N/m 590.85 Calculated Property
Property Value Unit Temperature (K) Source
λgas [0.01; 0.11] W/m×K [219.66; 1000.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A·T^B / (1 + C/T + D/T²)
Y is λgas in W/m×K, T in K
Coefficient A-6.54720e-02
Coefficient B2.77390e-01
Coefficient C-3.56920e+03
Coefficient D-1.62970e+06
Temperature range, min.219.66
Temperature range, max.1000.00
λgas 0.01 W/m×K 219.66 Calculated Property
λgas 0.01 W/m×K 306.36 Calculated Property
λgas 0.02 W/m×K 393.07 Calculated Property
λgas 0.03 W/m×K 479.77 Calculated Property
λgas 0.04 W/m×K 566.48 Calculated Property
λgas 0.05 W/m×K 653.18 Calculated Property
λgas 0.06 W/m×K 739.89 Calculated Property
λgas 0.07 W/m×K 826.59 Calculated Property
λgas 0.09 W/m×K 913.30 Calculated Property
λgas 0.11 W/m×K 1000.00 Calculated Property
Property Value Unit Temperature (K) Source
λliquid [0.15; 0.10] W/m×K [219.66; 423.97] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is λliquid in W/m×K, T in K
Coefficient A2.29980e-02
Coefficient B-2.32240e+01
Coefficient C-1.64750e+00
Coefficient D-6.33000e-04
Coefficient E-3.52110e-06
Temperature range, min.219.66
Temperature range, max.423.97
λliquid 0.15 W/m×K 219.66 Calculated Property
λliquid 0.15 W/m×K 242.36 Calculated Property
λliquid 0.14 W/m×K 265.06 Calculated Property
λliquid 0.13 W/m×K 287.76 Calculated Property
λliquid 0.13 W/m×K 310.46 Calculated Property
λliquid 0.12 W/m×K 333.17 Calculated Property
λliquid 0.12 W/m×K 355.87 Calculated Property
λliquid 0.11 W/m×K 378.57 Calculated Property
λliquid 0.10 W/m×K 401.27 Calculated Property
λliquid 0.10 W/m×K 423.97 Calculated Property

Similar Compounds

Triacontane. hexahexacontane. Heptadecane. Octane. pentacontane. Tetrapentacontane. Decane. Tridecane. heptapentacontane. heptacontane. Tetradecane. Dotriacontane. Pentadecane. Tetranonacontane. Heptacosane.

Find more compounds similar to Nonane.

Mixtures

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Sources

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