Chemical Properties of Pentane, 2,2,4-trimethyl- (CAS 540-84-1)

Pentane, 2,2,4-trimethyl-

InChI
InChI=1S/C8H18/c1-7(2)6-8(3,4)5/h7H,6H2,1-5H3
InChI Key
NHTMVDHEPJAVLT-UHFFFAOYSA-N
Formula
C8H18
SMILES
CC(C)CC(C)(C)C
Molecular Weight1
114.23
CAS
540-84-1
Other Names
  • (CH3)2CHCH2C(CH3)3
  • 2,2,4-trimethylpentane
  • Isobutyltrimethylethane
  • Isobutyltrimethylmethane
  • UN 1262
  • isooctane
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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 [0.3030; 0.3040]   Show Hide
ω 0.3030 PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω 0.3033 Passut and Danner (1973), critical constants and acentric factors Compiled value
ω 0.3040 ChemSep v8.3 pure component data Compiled value
ω 0.3030 KDB
AP 352.650 K KDB
ΔcH°liquid -5461.30 ± 1.30 kJ/mol NIST
μ 0.00 debye ChemSep v8.3 pure component data Compiled value
ΔfG° [13.69; 13.94] kJ/mol Show Hide
ΔfG° 13.94 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfG° 13.69 kJ/mol KDB
Rg 4.1710 KDB
Δc,grossH 5461.33 kJ/mol KDB
Δc,netH 5065.192 kJ/mol KDB
ΔfH°gas [-224.30; -223.70] kJ/mol Show Hide
ΔfH°gas -223.70 ± 1.50 kJ/mol Active Thermochemical Tables 1.112, gas-phase enthalpies of formation Compiled value
ΔfH°gas -224.01 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfH°gas -224.30 kJ/mol KDB
ΔfH°gas -224.10 ± 1.30 kJ/mol NIST
ΔfH°liquid -259.30 ± 1.30 kJ/mol NIST
ΔfusH° 5.54 kJ/mol Joback Calculated Property
ΔvapH° [34.90; 35.24] kJ/mol Show Hide
ΔvapH° 35.24 kJ/mol NIST
ΔvapH° Outlier 34.90 kJ/mol NIST
ΔvapH° 35.20 ± 0.10 kJ/mol NIST
ΔvapH° 35.10 ± 0.10 kJ/mol NIST
ΔvapH° 35.10 kJ/mol NIST
ΔvapH° 35.10 ± 0.10 kJ/mol NIST
ΔvapH° 35.12 kJ/mol NIST
IE [9.86; 9.91] eV Show Hide
IE 9.89 ± 0.03 eV NIST
IE 9.91 eV NIST
IE 9.86 eV NIST
log10WS [-4.74; -4.74]   Show Hide
log10WS -4.74 Aq. Solubility Prediction
log10WS -4.74 Estimated Solubility
logPoct/wat 3.079 Crippen Calculated Property
McVol 123.580 ml/mol McGowan Calculated Property
NFPA Fire 3 KDB
Pc [2564.33; 2583.79] kPa Show Hide
Pc 2570.00 kPa Critical Temperatures and Pressures of Several Binary and Ternary Mixtures Concerning the Alkylation of 2-Methylpropane with 1-Butene in the Presence of Methane or Carbon Dioxide
Pc 2570.00 kPa IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value
Pc 2569.60 kPa PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc 2567.61 kPa Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc 2570.00 kPa ChemSep v8.3 pure component data Compiled value
Pc 2570.00 kPa KDB
Pc 2570.00 ± 20.00 kPa NIST
Pc 2567.60 ± 40.53 kPa NIST
Pc 2564.33 ± 10.13 kPa NIST
Pc Outlier 2583.79 ± 15.19 kPa NIST
Ptriple 1.71e-05 kPa ChemSep v8.3 pure component data Compiled value
ρc [243.31; 244.45] kg/m3 Show Hide
ρc 244.45 ± 2.28 kg/m3 NIST
ρc 243.31 ± 4.57 kg/m3 NIST
ρc 243.31 ± 3.43 kg/m3 NIST
Inp [680.00; 703.10]   Show Hide
Inp 692.70 NIST
Inp 689.10 NIST
Inp 694.00 NIST
Inp 691.10 NIST
Inp 689.90 NIST
Inp 690.20 NIST
Inp 690.60 NIST
Inp 693.00 NIST
Inp Outlier 700.00 NIST
Inp 694.90 NIST
Inp 691.00 NIST
Inp 693.50 NIST
Inp Outlier 697.70 NIST
Inp Outlier 703.10 NIST
Inp 687.00 NIST
Inp 694.10 NIST
Inp 694.00 NIST
Inp 691.00 NIST
Inp 689.00 NIST
Inp 691.00 NIST
Inp 694.00 NIST
Inp 689.90 NIST
Inp 692.20 NIST
Inp 693.00 NIST
Inp 690.00 NIST
Inp 690.00 NIST
Inp 691.00 NIST
Inp 691.00 NIST
Inp 691.00 NIST
Inp 692.00 NIST
Inp 695.00 NIST
Inp 688.00 NIST
Inp 689.00 NIST
Inp 690.00 NIST
Inp 691.00 NIST
Inp 692.00 NIST
Inp 694.00 NIST
Inp 686.60 NIST
Inp 687.50 NIST
Inp 688.60 NIST
Inp 689.60 NIST
Inp 690.70 NIST
Inp 691.90 NIST
Inp 691.40 NIST
Inp 691.30 NIST
Inp 689.00 NIST
Inp 690.00 NIST
Inp 690.00 NIST
Inp 696.00 NIST
Inp 691.00 NIST
Inp 694.00 NIST
Inp 693.00 NIST
Inp 691.00 NIST
Inp 688.60 NIST
Inp 690.00 NIST
Inp 692.00 NIST
Inp 684.00 NIST
Inp 686.00 NIST
Inp 686.00 NIST
Inp 687.00 NIST
Inp 688.00 NIST
Inp 690.30 NIST
Inp 695.00 NIST
Inp Outlier 699.00 NIST
Inp 687.00 NIST
Inp 694.00 NIST
Inp 689.00 NIST
Inp 689.00 NIST
Inp 688.00 NIST
Inp 690.00 NIST
Inp 692.00 NIST
Inp 694.00 NIST
Inp 688.00 NIST
Inp 690.00 NIST
Inp 688.00 NIST
Inp 690.00 NIST
Inp 692.00 NIST
Inp 696.00 NIST
Inp 687.00 NIST
Inp 689.00 NIST
Inp 689.00 NIST
Inp 692.00 NIST
Inp 691.00 NIST
Inp 693.00 NIST
Inp 694.00 NIST
Inp 687.00 NIST
Inp 694.00 NIST
Inp 690.00 NIST
Inp Outlier 680.00 NIST
Inp 686.00 NIST
Inp 685.00 NIST
Inp 688.44 NIST
Inp 689.00 NIST
Inp 687.00 NIST
Inp 687.50 NIST
Inp 683.91 NIST
Inp 688.00 NIST
Inp 687.00 NIST
Inp 686.00 NIST
Inp 686.00 NIST
Inp 684.80 NIST
Inp 691.00 NIST
Inp 688.00 NIST
Inp 690.00 NIST
Inp 695.00 NIST
Inp 692.00 NIST
Inp 693.00 NIST
Inp 689.00 NIST
Inp 689.00 NIST
Inp 691.00 NIST
Inp 691.00 NIST
Inp 684.38 NIST
Inp 689.00 NIST
Inp 689.00 NIST
Inp 689.00 NIST
Inp 690.00 NIST
Inp 694.00 NIST
Inp 690.00 NIST
Inp 691.00 NIST
Inp 692.00 NIST
Inp 691.00 NIST
Inp 688.00 NIST
Inp 688.00 NIST
Inp 692.00 NIST
Inp 685.00 NIST
Inp 685.00 NIST
Inp 692.00 NIST
Inp 686.00 NIST
Inp Outlier 700.00 NIST
Inp Outlier 700.00 NIST
Inp 688.44 NIST
Inp 684.80 NIST
Inp 687.00 NIST
Inp 686.00 NIST
Inp 692.70 NIST
Inp 690.20 NIST
Inp 691.00 NIST
Inp 694.10 NIST
Inp 694.00 NIST
Inp 690.00 NIST
Inp 695.00 NIST
Inp 692.00 NIST
Inp 689.60 NIST
Inp 689.00 NIST
Inp 688.00 NIST
Ip [676.00; 711.00]   Show Hide
Ip 676.00 NIST
Ip 698.00 NIST
Ip 711.00 NIST
Ip 705.00 NIST
Ip 711.00 NIST
S°liquid [314.60; 328.03] J/mol×K Show Hide
S°liquid 328.03 J/mol×K NIST
S°liquid 314.60 J/mol×K NIST
Tboil [371.45; 389.00] K Show Hide
Tboil 372.33 K Vapor liquid equilibria for binary and ternary mixtures of diisopropyl ether, ethanol, and 2,2,4-trimethylpentane at 101.3 kPa
Tboil 372.33 K Measurements and correlation of vapour liquid equilibria of 2-butanone and hydrocarbons binary systems at two different pressures
Tboil 372.26 K Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Tboil 372.35 K Vapor-Liquid Equilibrium of Ferrocene in Some Organic Solvents Using Spectroscopic Methods
Tboil 372.39 K ChemSep v8.3 pure component data Compiled value
Tboil 372.37 K KDB
Tboil 372.40 ± 0.20 K NIST
Tboil 372.40 ± 0.20 K NIST
Tboil 372.40 K NIST
Tboil 372.40 K NIST
Tboil 372.00 ± 0.15 K NIST
Tboil 372.40 ± 0.15 K NIST
Tboil 372.50 ± 0.25 K NIST
Tboil 372.30 ± 0.30 K NIST
Tboil 372.15 ± 0.50 K NIST
Tboil 372.30 ± 0.50 K NIST
Tboil 372.35 ± 0.30 K NIST
Tboil 372.39 ± 0.20 K NIST
Tboil 371.45 ± 0.60 K NIST
Tboil 372.15 ± 0.40 K NIST
Tboil 372.30 ± 0.20 K NIST
Tboil 372.40 ± 0.60 K NIST
Tboil 372.37 ± 0.20 K NIST
Tboil 372.38 ± 0.05 K NIST
Tboil 372.39 ± 0.10 K NIST
Tboil 372.65 ± 2.00 K NIST
Tboil 372.15 ± 2.00 K NIST
Tboil 372.35 ± 0.40 K NIST
Tboil 372.45 ± 0.30 K NIST
Tboil 372.50 ± 0.40 K NIST
Tboil 372.38 ± 0.27 K NIST
Tboil 372.38 ± 0.20 K NIST
Tboil 372.38 ± 0.15 K NIST
Tboil 372.45 ± 0.50 K NIST
Tboil 372.38 ± 0.10 K NIST
Tboil 372.38 ± 0.01 K NIST
Tboil 372.39 ± 0.25 K NIST
Tboil 372.38 ± 0.10 K NIST
Tboil 372.45 ± 0.50 K NIST
Tboil 372.39 ± 0.07 K NIST
Tboil 372.50 ± 0.20 K NIST
Tboil 372.55 ± 0.20 K NIST
Tboil 372.39 ± 0.05 K NIST
Tboil 372.38 ± 0.05 K NIST
Tboil 372.39 ± 0.20 K NIST
Tboil 372.55 ± 0.30 K NIST
Tboil 372.38 ± 0.03 K NIST
Tboil 372.25 ± 0.50 K NIST
Tboil 372.25 ± 0.20 K NIST
Tboil 372.38 ± 0.10 K NIST
Tboil 372.38 ± 0.10 K NIST
Tboil 372.40 ± 0.40 K NIST
Tboil 372.25 ± 0.20 K NIST
Tboil 372.65 ± 2.00 K NIST
Tboil 372.35 ± 0.50 K NIST
Tboil 372.45 ± 0.40 K NIST
Tboil 372.45 ± 0.50 K NIST
Tboil Outlier 389.00 ± 2.00 K NIST
Tc [543.61; 544.30] K Show Hide
Tc 544.00 K The Critical Temperatures of a Number of (i) (Chloroalkane (C3 C4) + Hydrocarbon (C6 C7)) Binary Mixtures and (ii) (Aromatic Halocarbon (Chlorobenzene, Fluorobenzene, 1,2-Dichlorobenzene, or 1,3-Dichlorobenzene) + Alkane (C8)) Binary Mixtures
Tc 543.80 K IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value
Tc 543.80 K PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc 543.96 K Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc 543.90 K ChemSep v8.3 pure component data Compiled value
Tc 543.80 K KDB
Tc 543.80 ± 0.30 K NIST
Tc 543.90 K NIST
Tc 543.89 ± 0.40 K NIST
Tc 543.61 ± 0.20 K NIST
Tc 543.82 ± 0.10 K NIST
Tc Outlier 544.30 ± 0.20 K NIST
Tfus [165.00; 166.15] K Show Hide
Tfus Outlier 166.15 K Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus 165.78 K ChemSep v8.3 pure component data Compiled value
Tfus 165.80 K KDB
Tfus 166.07 K Aq. Solubility Prediction
Tfus 165.78 ± 0.10 K NIST
Tfus 165.75 ± 0.04 K NIST
Tfus 165.76 ± 0.02 K NIST
Tfus 165.75 ± 0.02 K NIST
Tfus 165.76 ± 0.02 K NIST
Tfus 165.73 ± 0.10 K NIST
Tfus 165.73 ± 0.10 K NIST
Tfus 165.73 ± 0.10 K NIST
Tfus 165.73 ± 0.06 K NIST
Tfus 165.73 ± 0.06 K NIST
Tfus 165.73 ± 0.06 K NIST
Tfus 165.77 ± 0.09 K NIST
Tfus 165.77 ± 0.05 K NIST
Tfus 165.76 ± 0.06 K NIST
Tfus 165.76 ± 0.03 K NIST
Tfus 165.85 ± 0.20 K NIST
Tfus 165.73 ± 0.10 K NIST
Tfus 165.76 ± 0.06 K NIST
Tfus 165.75 ± 0.15 K NIST
Tfus 165.76 ± 0.03 K NIST
Tfus 165.77 ± 0.02 K NIST
Tfus 165.73 ± 0.15 K NIST
Tfus 165.75 ± 0.30 K NIST
Tfus 165.75 ± 0.12 K NIST
Tfus 165.77 ± 0.05 K NIST
Tfus 165.78 ± 0.03 K NIST
Tfus 165.75 ± 0.04 K NIST
Tfus 165.77 ± 0.02 K NIST
Tfus 165.78 ± 0.20 K NIST
Tfus 165.75 ± 0.01 K NIST
Tfus 165.83 ± 0.30 K NIST
Tfus 165.83 ± 0.30 K NIST
Tfus 165.75 ± 0.50 K NIST
Tfus 165.78 ± 0.20 K NIST
Tfus 165.78 ± 0.07 K NIST
Tfus 165.55 ± 0.40 K NIST
Tfus 165.83 ± 0.20 K NIST
Tfus 165.55 ± 0.20 K NIST
Tfus 165.84 ± 0.06 K NIST
Tfus Outlier 166.15 ± 2.00 K NIST
Tfus Outlier 165.00 ± 2.00 K NIST
Tfus 165.65 ± 0.50 K NIST
Tfus 165.45 ± 0.40 K NIST
Tfus Outlier 165.35 ± 0.50 K NIST
Ttriple [165.30; 165.85] K Show Hide
Ttriple 165.85 K Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple 165.78 K ChemSep v8.3 pure component data Compiled value
Ttriple 165.76 ± 0.40 K NIST
Ttriple 165.30 ± 0.20 K NIST
Ttriple 165.30 ± 0.20 K NIST
UQi 4.94 ChemSep v8.3 pure component data Compiled value
URi 5.85 ChemSep v8.3 pure component data Compiled value
Vc [0.468; 0.482] m3/kmol Show Hide
Vc 0.468 m3/kmol IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value
Vc 0.468 m3/kmol PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc 0.470 m3/kmol ChemSep v8.3 pure component data Compiled value
Vc 0.468 m3/kmol KDB
Vc 0.468 m3/kmol NIST
Vc Outlier 0.482 ± 0.020 m3/kmol NIST
VCOSTALD 0.48 m3/kmol Hankinson and Thomson (1979), COSTALD parameters Compiled value
ωSRK 0.30 Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zc [0.2660000; 0.2670000]   Show Hide
Zc 0.2670000 IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value
Zc 0.2660000 ChemSep v8.3 pure component data Compiled value
Zc 0.2660130 KDB
Zra [0.27; 0.27]   Show Hide
Zra 0.27 Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zra 0.27 KDB

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,liquid [186.00; 275.50] J/mol×K [170.00; 370.00] Show Hide
Cp,liquid 186.00 J/mol×K 170.00 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 189.20 J/mol×K 180.00 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 192.60 J/mol×K 190.00 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 196.20 J/mol×K 200.00 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 199.90 J/mol×K 210.00 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 203.80 J/mol×K 220.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 207.80 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 211.90 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 216.20 J/mol×K 250.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 220.70 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 225.20 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 226.70 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 229.90 J/mol×K 280.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 234.60 J/mol×K 290.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 237.85 J/mol×K 293.15 NIST
Cp,liquid 233.90 J/mol×K 295.20 NIST
Cp,liquid 242.49 J/mol×K 298.15 NIST
Cp,liquid 237.80 J/mol×K 298.15 NIST
Cp,liquid 238.60 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 238.57 J/mol×K 298.15 NIST
Cp,liquid 237.80 J/mol×K 298.15 NIST
Cp,liquid 238.87 J/mol×K 298.15 NIST
Cp,liquid 239.71 J/mol×K 298.15 NIST
Cp,liquid 242.49 J/mol×K 298.15 NIST
Cp,liquid 239.50 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 233.70 J/mol×K 300.00 NIST
Cp,liquid 241.00 J/mol×K 301.90 NIST
Cp,liquid 244.40 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 249.40 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 254.50 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 259.70 J/mol×K 340.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 264.90 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 270.20 J/mol×K 360.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 275.50 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 [0.0003690; 0.0005439] Pa×s [288.15; 323.15] Show Hide
η 0.0005439 Pa×s 288.15 Densities and viscosities of binary and ternary mixtures of cyclohexanone, 1,4-dioxane and isooctane from T = (288.15 to 313.15) K
η 0.0005125 Pa×s 293.15 Densities and viscosities of binary and ternary mixtures of cyclohexanone, 1,4-dioxane and isooctane from T = (288.15 to 313.15) K
η 0.0004844 Pa×s 298.15 Densities and viscosities of binary and ternary mixtures of cyclohexanone, 1,4-dioxane and isooctane from T = (288.15 to 313.15) K
η 0.0004780 Pa×s 298.15 Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
η 0.0004586 Pa×s 303.15 Densities and viscosities of binary and ternary mixtures of cyclohexanone, 1,4-dioxane and isooctane from T = (288.15 to 313.15) K
η 0.0004530 Pa×s 303.15 Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
η 0.0004216 Pa×s 308.15 Densities and viscosities of binary and ternary mixtures of cyclohexanone, 1,4-dioxane and isooctane from T = (288.15 to 313.15) K
η 0.0004290 Pa×s 308.15 Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
η 0.0004130 Pa×s 313.15 Densities and viscosities of binary and ternary mixtures of cyclohexanone, 1,4-dioxane and isooctane from T = (288.15 to 313.15) K
η 0.0004080 Pa×s 313.15 Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
η 0.0003880 Pa×s 318.15 Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
η 0.0003690 Pa×s 323.15 Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
ΔfusH [9.04; 9.21] kJ/mol [165.30; 165.80] Show Hide
ΔfusH 9.04 kJ/mol 165.30 NIST
ΔfusH 9.04 kJ/mol 165.30 NIST
ΔfusH 9.04 kJ/mol 165.30 NIST
ΔfusH 9.04 kJ/mol 165.30 NIST
ΔfusH 9.21 kJ/mol 165.79 NIST
ΔfusH 9.20 kJ/mol 165.80 NIST
ΔvapH [30.79; 40.70] kJ/mol [246.50; 517.00] Show Hide
ΔvapH 40.70 kJ/mol 246.50 NIST
ΔvapH 36.10 kJ/mol 311.00 NIST
ΔvapH 34.40 ± 0.10 kJ/mol 313.00 NIST
ΔvapH 34.30 ± 0.10 kJ/mol 313.00 NIST
ΔvapH 33.40 ± 0.10 kJ/mol 328.00 NIST
ΔvapH 33.20 ± 0.10 kJ/mol 333.00 NIST
ΔvapH 34.80 kJ/mol 335.50 NIST
ΔvapH 32.60 ± 0.10 kJ/mol 343.00 NIST
ΔvapH 32.00 ± 0.10 kJ/mol 353.00 NIST
ΔvapH 31.70 ± 0.10 kJ/mol 358.00 NIST
ΔvapH 33.90 kJ/mol 358.50 NIST
ΔvapH 31.00 ± 0.10 kJ/mol 368.00 NIST
ΔvapH 31.00 kJ/mol 371.00 NIST
ΔvapH 31.01 kJ/mol 372.40 KDB
ΔvapH 30.79 kJ/mol 372.40 NIST
ΔvapH 32.20 kJ/mol 394.00 NIST
ΔvapH 31.50 kJ/mol 453.50 NIST
ΔvapH 31.60 kJ/mol 473.00 NIST
ΔvapH 31.40 kJ/mol 517.00 NIST
ν [0.0000005; 0.0000007] m2/s [293.15; 323.15] Show Hide
ν 0.0000007 m2/s 293.15 Density, Viscosity, and Speed of Sound of Solutions of AOT Reverse Micelles in 2,2,4-Trimethylpentane
ν 0.0000007 m2/s 298.15 Density, Viscosity, and Speed of Sound of Solutions of AOT Reverse Micelles in 2,2,4-Trimethylpentane
ν 0.0000007 m2/s 303.15 Density, Viscosity, and Speed of Sound of Solutions of AOT Reverse Micelles in 2,2,4-Trimethylpentane
ν 0.0000006 m2/s 313.15 Density, Viscosity, and Speed of Sound of Solutions of AOT Reverse Micelles in 2,2,4-Trimethylpentane
ν 0.0000005 m2/s 323.15 Density, Viscosity, and Speed of Sound of Solutions of AOT Reverse Micelles in 2,2,4-Trimethylpentane
Pvap [3.05; 282.80] kPa [283.60; 413.15] Show Hide
Pvap 3.05 kPa 283.60 A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap 3.99 kPa 288.40 A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap 5.18 kPa 293.40 A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap 6.63 kPa 298.30 A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap 6.62 kPa 298.40 A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap 8.33 kPa 303.15 Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
Pvap 8.39 kPa 303.30 A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap 10.44 kPa 308.15 Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
Pvap 10.53 kPa 308.20 A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap 12.97 kPa 313.10 A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap 12.95 kPa 313.15 Vapour-liquid equilibria of binary and ternary mixtures containing 1-butanol, 2,2,4-trimethylpentane and 1-hexene at T = 313.15 K
Pvap 12.95 kPa 313.15 Phase equilibrium properties of binary and ternary mixtures containing 2-butanol, 2,2,4- trimethylpentane and 1-hexene at 313.15 K
Pvap 13.01 kPa 313.15 Vapor-Liquid Equilibria of Binary Mixtures Containing 1-Butanol and Hydrocarbons at 313.15 K
Pvap 12.96 kPa 313.15 Vapor Liquid Equilibria of Binary Mixtures Containing 2-Butanol and Hydrocarbons at 313.15 K
Pvap 12.97 kPa 313.15 Thermodynamic behaviour of second generation biofuels: Vapour liquid equilibria and excess enthalpies of the binary mixtures 2-pentanol and n-heptane or 2,2,4-trimethylpentane
Pvap 12.97 kPa 313.15 Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
Pvap 15.96 kPa 318.10 A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap 15.98 kPa 318.15 Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
Pvap 19.54 kPa 323.00 A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap 19.54 kPa 323.15 Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
Pvap 20.00 kPa 323.65 Measurements and correlation of vapour liquid equilibria of 2-butanone and hydrocarbons binary systems at two different pressures
Pvap 23.81 kPa 328.00 A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap 28.66 kPa 332.80 A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
Pvap 100.05 kPa 371.55 Isobaric Vapor Liquid Equilibrium for Binary Systems of 2,2,4-Trimethylpentane with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 250 kPa
Pvap 101.30 kPa 372.26 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 101.30 kPa 372.33 Measurements and correlation of vapour liquid equilibria of 2-butanone and hydrocarbons binary systems at two different pressures
Pvap 101.33 kPa 372.35 Vapor-Liquid Equilibrium of Ferrocene in Some Organic Solvents Using Spectroscopic Methods
Pvap 103.49 kPa 373.10 Phase Equilibria on Four Binary Systems: 1,2-Dichloroethane + trans-1,2-Dichloroethylene, 1-Octene + 2-Methyl Thiophene, 2-Ethyl Thiophene + 2,2,4-Trimethylpentane, and Cyclopropanecarbonitrile + Water
Pvap 104.94 kPa 373.40 Isobaric Vapor Liquid Equilibrium for Binary Systems of 2,2,4-Trimethylpentane with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 250 kPa
Pvap 124.90 kPa 379.80 Isobaric Vapor Liquid Equilibrium for Binary Systems of 2,2,4-Trimethylpentane with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 250 kPa
Pvap 149.96 kPa 386.94 Isobaric Vapor Liquid Equilibrium for Binary Systems of 2,2,4-Trimethylpentane with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 250 kPa
Pvap 174.70 kPa 393.14 Isobaric Vapor Liquid Equilibrium for Binary Systems of 2,2,4-Trimethylpentane with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 250 kPa
Pvap 199.94 kPa 398.64 Isobaric Vapor Liquid Equilibrium for Binary Systems of 2,2,4-Trimethylpentane with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 250 kPa
Pvap 224.91 kPa 403.68 Isobaric Vapor Liquid Equilibrium for Binary Systems of 2,2,4-Trimethylpentane with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 250 kPa
Pvap 249.95 kPa 408.28 Isobaric Vapor Liquid Equilibrium for Binary Systems of 2,2,4-Trimethylpentane with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 250 kPa
Pvap 250.00 kPa 408.30 Isobaric Vapor Liquid Equilibrium for Binary Systems of 2,2,4-Trimethylpentane with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 250 kPa
Pvap 282.80 kPa 413.15 Phase Equilibria on Four Binary Systems: 1,2-Dichloroethane + trans-1,2-Dichloroethylene, 1-Octene + 2-Methyl Thiophene, 2-Ethyl Thiophene + 2,2,4-Trimethylpentane, and Cyclopropanecarbonitrile + Water
n0 [1.37898; 1.39404]   [288.15; 318.15] Show Hide
n0 1.39404 288.15 Densities, Refractive indices and Viscosities for Binary and Ternary Mixtures of Acetone, Ethanol and 2,2,4-Trimethylpentane at T = (288.15, 298.15, and 308.15) K
n0 1.39404 288.15 Densities, Viscosities, and Refractive Indices for Binary and Ternary Mixtures of Diisopropyl Ether, Ethanol, and 2,2,4-Trimethylpentane
n0 1.38894 293.15 Isothermal Vapor-Liquid Equilibria in the Two Binary and the Ternary Systems Composed of tert-Amyl Methyl Ether, tert-Butanol, and Isooctane
n0 1.38921 298.10 Liquid-Liquid Equilibria for [C8mim][NTf2] + Thiophene + 2,2,4-Trimethylpentane or + Toluene
n0 1.38900 298.15 A Study on Alkane + Ester + Ester Systems. Physicochemical Behavior of Binaries and Ternaries of Octane or Iso-octane with Methyl Esters (Ethanoate, Butanoate, Pentanoate)
n0 1.38902 298.15 Densities and Viscosities for Binary and Ternary Mixtures of Ethanol, 2-Butanone, and 2,2,4-Trimethylpentane at T = (298.15, 308.15, and 318.15) K
n0 1.38890 298.15 Phase equilibria on four binary systems containing 3-methylthiophene
n0 1.38890 298.15 Excess molar volumes, excess molar enthalpies and refractive index deviations for binary mixtures of propan-1-ol, butan-1-ol and pentan-1-ol with 2,2,4-trimethylpentane at 298.15 K
n0 1.38800 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 1.38898 298.15 KDB
n0 1.38887 298.15 Vapor liquid equilibria for binary and ternary mixtures of ethanol, 2-butanone, and 2,2,4-trimethylpentane at 101.3 kPa
n0 1.38890 298.15 (Vapor + liquid) equilibria of binary mixtures formed by iso-octane with a variety of compounds at 95.8 kPa
n0 1.38905 298.15 Volumetric behaviour of binary liquid systems composed of toluene, isooctane, and methyl tert-butyl ether at temperatures from (298.15 to 328.15) K
n0 1.38894 298.15 Isothermal (vapour + liquid) equilibria in the binary and ternary systems composed of 2-propanol, 2,2,4-trimethylpentane, and 2,4-dimethyl-3-pentanone
n0 1.38904 298.15 (Vapour + liquid) equilibria for binary and ternary mixtures of 2-propanol, tetrahydropyran, and 2,2,4-trimethylpentane at P = 101.3 kPa
n0 1.38901 298.15 Volumetric behaviour of the (2,2,4-trimethylpentane + methylbenzene + butan-1-ol) ternary system and its binary sub-systems within the temperature range (298.15-328.15) K
n0 1.38887 298.15 Isobaric vapor liquid equilibria for mixtures of acetone, ethanol, and 2,2,4-trimethylpentane at 101.3 kPa
n0 1.38887 298.15 Vapor-Liquid Equilibria for Binary and Ternary Mixtures of 1,3-Dioxolane, 2-Propanol, and 2,2,4-Trimethylpentane at 101.3 kPa
n0 1.38905 298.15 Measurement of VLE Data by Using an Experimental Installation with Automatic Control: Modeling of Binary Systems of Methyl Acetate or Ethyl Acetate with n-Heptane or 2,2,4-Trimethylpentane at Both 0.1 and 1.5 MPa
n0 1.38898 298.15 Isothermal vapor liquid equilibrium at 333.15K and excess molar volumes and refractive indices at 298.15K for the mixtures of di-methyl carbonate, ethanol and 2,2,4-trimethylpentane
n0 1.38917 298.15 Liquid liquid equilibria of lactam containing binary systems
n0 1.38900 298.15 Densities, Refractive indices and Viscosities for Binary and Ternary Mixtures of Acetone, Ethanol and 2,2,4-Trimethylpentane at T = (288.15, 298.15, and 308.15) K
n0 1.38900 298.15 Vapor liquid equilibrium for binary system of thiophene + 2,2,4-trimethylpentane at 343.15 and 353.15K and thiophene + 2-ethoxy-2-methylpropane at 333.15 and 343.15K
n0 1.38898 298.15 Densities, Viscosities, and Refractive Indices for Binary and Ternary Mixtures of Ethanol, 2-Methylpropan-2-ol, and 2,2,4-Trimethylpentane
n0 1.38920 298.15 Isothermal Vapor Liquid Equilibrium Data of Propan-1-ol + 2,2,4-Trimethylpentane and Butan-1-ol + 2,2,4-Trimethylpentane at 318.15 K
n0 1.38900 298.15 Vapor-Liquid Equilibrium for Binary System of Diethyl Sulfide + n-Heptane and Diethyl Sulfide + 2,2,4-Trimethylpentane at (363.15 and 353.15) K
n0 1.38894 298.15 Isothermal vapour liquid equilibria in the binary and ternary systems composed of 2-propanol, 3-methyl-2-butanone and 2,2,4-trimethylpentane
n0 1.38900 298.15 Densities, Viscosities, and Refractive Indices for Binary and Ternary Mixtures of Diisopropyl Ether, Ethanol, and 2,2,4-Trimethylpentane
n0 1.38910 298.20 Vapor-Liquid Equilibrium Measurements of Ether Alcohol Blends for Investigation on Reformulated Gas
n0 1.38520 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 1.38395 308.15 Densities, Viscosities, and Refractive Indices for Binary and Ternary Mixtures of Diisopropyl Ether, Ethanol, and 2,2,4-Trimethylpentane
n0 1.38398 308.15 Densities, Viscosities, and Refractive Indices for Binary and Ternary Mixtures of Ethanol, 2-Methylpropan-2-ol, and 2,2,4-Trimethylpentane
n0 1.38395 308.15 Densities, Refractive indices and Viscosities for Binary and Ternary Mixtures of Acetone, Ethanol and 2,2,4-Trimethylpentane at T = (288.15, 298.15, and 308.15) K
n0 1.38240 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 1.37898 318.15 Densities, Viscosities, and Refractive Indices for Binary and Ternary Mixtures of Ethanol, 2-Methylpropan-2-ol, and 2,2,4-Trimethylpentane
ρl [649.40; 704.10] kg/m3 [278.15; 343.15] Show Hide
ρl 704.10 kg/m3 278.15 Advanced calibration, adjustment, and operation of a density and sound speed analyzer
ρl 700.05 kg/m3 283.15 Advanced calibration, adjustment, and operation of a density and sound speed analyzer
ρl 695.98 kg/m3 288.15 Advanced calibration, adjustment, and operation of a density and sound speed analyzer
ρl 692.00 kg/m3 293.00 KDB
ρl 691.88 kg/m3 293.00 Volumetric behavior of the binary systems benzene + cyclohexane and benzene + 2,2,4-trimethyl-pentane at temperatures 293.15-323.15K
ρl 692.00 kg/m3 293.15 Experimental Solubility Data for Binary Mixtures of Ethane and 2,2,4-Trimethylpentane at Pressures up to 6 MPa Using a New Variable-Volume Sapphire Cell
ρl 691.89 kg/m3 293.15 Excess molar volume along with viscosity, refractive index and relative permittivity for binary mixtures of exo-tetrahydrodicyclopentadiene with four octane isomers
ρl 691.91 kg/m3 293.15 Densities, Viscosities, Refractive Indices, and Surface Tensions of Binary Mixtures of 2,2,4-Trimethylpentane with Several Alkylated Cyclohexanes from (293.15 to 343.15) K
ρl 691.84 kg/m3 293.15 Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
ρl 691.83 kg/m3 293.15 Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
ρl 692.05 kg/m3 293.15 Isothermal Binary and Ternary VLE for the Mixtures of Propyl Vinyl Ether + Ethanol + Isooctane at 323.15 K and VE at 293.15 K
ρl 691.89 kg/m3 293.15 Advanced calibration, adjustment, and operation of a density and sound speed analyzer
ρl 690.40 kg/m3 295.00 High-pressure vapor-liquid equilibria of the second generation biofuel blends (2-methylfuran + iso-octane) and (2-methyltetrahydrofuran + di-n-butyl ether): Experiments and PCP-SAFT modeling
ρl 687.82 kg/m3 298.15 Isobaric vapor-liquid equilibrium, density and speed of sound of binary mixtures 2,2,4-trimethylpentane + 1-butanol or dibutyl ether (DBE) at 101.3 kPa
ρl 688.03 kg/m3 298.15 Excess enthalpies of binary mixtures of 1-hexene with some branched alkanes at the temperature 298.15 K
ρl 687.62 kg/m3 298.15 Excess Volumes of Ternary Mixtures 2,2,4-Trimethylpentane + Diisopropyl Ether or Methyl tert-Butyl Ether + Methanol, Ethanol, or 1-Propanol at 298.15 K
ρl 687.82 kg/m3 298.15 Densities, Viscosities, Refractive Indices, and Surface Tensions of Binary Mixtures of 2,2,4-Trimethylpentane with Several Alkylated Cyclohexanes from (293.15 to 343.15) K
ρl 687.72 kg/m3 298.15 Phase equilibria for binary systems of octane boosters with 2,2,4-trimethylpentane
ρl 687.77 kg/m3 298.15 Advanced calibration, adjustment, and operation of a density and sound speed analyzer
ρl 687.70 kg/m3 298.15 Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
ρl 688.18 kg/m3 298.15 Binary LLE for Propyl Vinyl Ether (PVE) + Water, Ternary LLE for PVE + Methanol or Ethanol + Water at 298.15 K, and VE and centsR at 293.15 K for the Mixture of PVE + Ethanol + 2,2,4-Trimethylpentane
ρl 687.91 kg/m3 298.15 Liquid Liquid Equilibrium for Ternary Systems of Propyl Vinyl Ether + C3 or C4 Alcohols + Water at 298.15 K and Excess Molar Enthalpies for Ternary and Constituent Binary Systems of Propyl Vinyl Ether + Ethanol + Isooctane at 303.15 K
ρl 687.77 kg/m3 298.15 Thermodynamics of Mixtures Containing a Very Strongly Polar Compound. 10. Liquid Liquid Equilibria for N,N-Dimethylacetamide + Selected Alkanes
ρl 687.32 kg/m3 298.15 Thermodynamics of aromatic polar compound (alkanone, alkanal or alkanoate) + hydrocarbon mixtures
ρl 687.75 kg/m3 298.15 Excess molar volume along with viscosity, refractive index and relative permittivity for binary mixtures of exo-tetrahydrodicyclopentadiene with four octane isomers
ρl 687.32 kg/m3 298.15 Liquid-Liquid Equilibria for 2-Phenylethan-1-ol + Alkane Systems
ρl 687.76 kg/m3 298.15 Thermodynamics of Mixtures Containing a Strongly Polar Compound. 9. Liquid-Liquid Equilibria for epsilon-Caprolactam + Selected Alkanes
ρl 687.81 kg/m3 298.15 Liquid Liquid Equilibria, Equilibrium Phase Densities, and Refractive Indices for the Quaternary Mixtures Containing 2-Propanol or 2-Methyl-2-Propanol of Fuel Oxygenate at T = 298.15 and 318.15 K
ρl 687.74 kg/m3 298.15 Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
ρl 687.72 kg/m3 298.20 Apparent and Partial Molar Volumes at Infinite Dilution and Solid Liquid Equilibria of Dibenzothiophene + Alkane Systems
ρl 683.64 kg/m3 303.00 Volumetric behavior of the binary systems benzene + cyclohexane and benzene + 2,2,4-trimethyl-pentane at temperatures 293.15-323.15K
ρl 683.64 kg/m3 303.15 Advanced calibration, adjustment, and operation of a density and sound speed analyzer
ρl 683.68 kg/m3 303.15 Densities, Viscosities, Refractive Indices, and Surface Tensions of Binary Mixtures of 2,2,4-Trimethylpentane with Several Alkylated Cyclohexanes from (293.15 to 343.15) K
ρl 683.59 kg/m3 303.15 Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
ρl 683.61 kg/m3 303.15 Excess molar volume along with viscosity, refractive index and relative permittivity for binary mixtures of exo-tetrahydrodicyclopentadiene with four octane isomers
ρl 683.74 kg/m3 303.15 Isothermal VLE and VE at 303.15 K for the Binary and Ternary Mixtures of Di-isopropyl Ether (DIPE) + 1-Propanol + 2,2,4-Trimethylpentane
ρl 683.61 kg/m3 303.15 Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
ρl 679.48 kg/m3 308.15 Advanced calibration, adjustment, and operation of a density and sound speed analyzer
ρl 679.51 kg/m3 308.15 Densities, Viscosities, Refractive Indices, and Surface Tensions of Binary Mixtures of 2,2,4-Trimethylpentane with Several Alkylated Cyclohexanes from (293.15 to 343.15) K
ρl 679.47 kg/m3 308.15 Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
ρl 679.44 kg/m3 308.15 Excess molar volume along with viscosity, refractive index and relative permittivity for binary mixtures of exo-tetrahydrodicyclopentadiene with four octane isomers
ρl 679.40 kg/m3 308.15 Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
ρl 675.30 kg/m3 313.00 Volumetric behavior of the binary systems benzene + cyclohexane and benzene + 2,2,4-trimethyl-pentane at temperatures 293.15-323.15K
ρl 675.28 kg/m3 313.15 Advanced calibration, adjustment, and operation of a density and sound speed analyzer
ρl 675.32 kg/m3 313.15 Densities, Viscosities, Refractive Indices, and Surface Tensions of Binary Mixtures of 2,2,4-Trimethylpentane with Several Alkylated Cyclohexanes from (293.15 to 343.15) K
ρl 675.23 kg/m3 313.15 Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
ρl 675.29 kg/m3 313.15 Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
ρl 675.25 kg/m3 313.15 Excess molar volume along with viscosity, refractive index and relative permittivity for binary mixtures of exo-tetrahydrodicyclopentadiene with four octane isomers
ρl 675.23 kg/m3 313.20 Apparent and Partial Molar Volumes at Infinite Dilution and Solid Liquid Equilibria of Dibenzothiophene + Alkane Systems
ρl 671.07 kg/m3 318.15 Advanced calibration, adjustment, and operation of a density and sound speed analyzer
ρl 670.98 kg/m3 318.15 Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
ρl 671.05 kg/m3 318.15 Densities, Viscosities, Refractive Indices, and Surface Tensions of Binary Mixtures of 2,2,4-Trimethylpentane with Several Alkylated Cyclohexanes from (293.15 to 343.15) K
ρl 671.09 kg/m3 318.15 Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
ρl 666.84 kg/m3 323.00 Volumetric behavior of the binary systems benzene + cyclohexane and benzene + 2,2,4-trimethyl-pentane at temperatures 293.15-323.15K
ρl 666.80 kg/m3 323.15 Densities, Viscosities, Refractive Indices, and Surface Tensions of Binary Mixtures of 2,2,4-Trimethylpentane with Several Alkylated Cyclohexanes from (293.15 to 343.15) K
ρl 666.81 kg/m3 323.15 Advanced calibration, adjustment, and operation of a density and sound speed analyzer
ρl 666.75 kg/m3 323.15 Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
ρl 666.86 kg/m3 323.15 Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
ρl 662.44 kg/m3 328.15 Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
ρl 662.52 kg/m3 328.15 Advanced calibration, adjustment, and operation of a density and sound speed analyzer
ρl 658.20 kg/m3 333.15 Densities, Viscosities, Refractive Indices, and Surface Tensions of Binary Mixtures of 2,2,4-Trimethylpentane with Several Alkylated Cyclohexanes from (293.15 to 343.15) K
ρl 658.16 kg/m3 333.15 Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
ρl 658.19 kg/m3 333.15 Advanced calibration, adjustment, and operation of a density and sound speed analyzer
ρl 653.80 kg/m3 338.15 Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
ρl 653.81 kg/m3 338.15 Advanced calibration, adjustment, and operation of a density and sound speed analyzer
ρl 649.40 kg/m3 343.15 Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
ρl 649.40 kg/m3 343.15 Advanced calibration, adjustment, and operation of a density and sound speed analyzer
ρl 649.44 kg/m3 343.15 Densities, Viscosities, Refractive Indices, and Surface Tensions of Binary Mixtures of 2,2,4-Trimethylpentane with Several Alkylated Cyclohexanes from (293.15 to 343.15) K
ΔfusS [54.70; 55.56] J/mol×K [165.30; 165.79] Show Hide
ΔfusS 54.70 J/mol×K 165.30 NIST
ΔfusS 54.70 J/mol×K 165.30 NIST
ΔfusS 55.56 J/mol×K 165.79 NIST
csound,fluid [979.25; 1124.31] m/s [288.15; 323.15] Show Hide
csound,fluid 1124.31 m/s 288.15 Temperature influence on mixing properties of {ethyl tert-butyl ether (ETBE) + gasoline additives}
csound,fluid 1124.31 m/s 288.15 Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid 1113.83 m/s 290.65 Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid 1103.30 m/s 293.15 Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid 1092.66 m/s 295.65 Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid 1082.20 m/s 298.15 Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid 1082.20 m/s 298.15 Temperature influence on mixing properties of {ethyl tert-butyl ether (ETBE) + gasoline additives}
csound,fluid 1071.72 m/s 300.65 Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid 1061.30 m/s 303.15 Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid 1050.89 m/s 305.65 Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid 1040.53 m/s 308.15 Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid 1030.22 m/s 310.65 Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid 1019.94 m/s 313.15 Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid 1009.71 m/s 315.65 Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid 999.53 m/s 318.15 Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid 989.37 m/s 320.65 Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid 979.25 m/s 323.15 Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid 979.25 m/s 323.15 Temperature influence on mixing properties of {ethyl tert-butyl ether (ETBE) + gasoline additives}
γ [0.02; 0.02] N/m [288.15; 323.15] Show Hide
γ 0.02 N/m 288.15 Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ 0.02 N/m 288.15 Densities, Viscosities, Refractive Indexes, and Surface Tensions for Binary and Ternary Mixtures of Tetrahydofuran, 2-Propanol, and 2,2,4-Trimethylpentane
γ 0.02 N/m 288.15 Densities, Viscosities, Refractive Indices, and Surface Tensions for the Mixtures of 1,3-Dioxolane + 2-Propanol or + 2,2,4-Trimethylpentane at (288.15, 298.15, and 308.15) K and 1,3-Dioxolane + 2-Propanol + 2,2,4-Trimethylpentane at 298.15 K
γ 0.02 N/m 298.15 Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ 0.02 N/m 298.15 Densities, Viscosities, Refractive Indexes, and Surface Tensions for Binary and Ternary Mixtures of Tetrahydofuran, 2-Propanol, and 2,2,4-Trimethylpentane
γ 0.02 N/m 298.15 Densities, Viscosities, Refractive Indices, and Surface Tensions for the Mixtures of 1,3-Dioxolane + 2-Propanol or + 2,2,4-Trimethylpentane at (288.15, 298.15, and 308.15) K and 1,3-Dioxolane + 2-Propanol + 2,2,4-Trimethylpentane at 298.15 K
γ 0.02 N/m 298.20 KDB
γ 0.02 N/m 303.15 Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ 0.02 N/m 308.15 Densities, Viscosities, Refractive Indices, and Surface Tensions for the Mixtures of 1,3-Dioxolane + 2-Propanol or + 2,2,4-Trimethylpentane at (288.15, 298.15, and 308.15) K and 1,3-Dioxolane + 2-Propanol + 2,2,4-Trimethylpentane at 298.15 K
γ 0.02 N/m 308.15 Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ 0.02 N/m 308.15 Densities, Viscosities, Refractive Indexes, and Surface Tensions for Binary and Ternary Mixtures of Tetrahydofuran, 2-Propanol, and 2,2,4-Trimethylpentane
γ 0.02 N/m 313.15 Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ 0.02 N/m 318.15 Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ 0.02 N/m 323.15 Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
λliquid [0.09; 0.10] W/m×K [259.11; 328.14] Show Hide
λliquid 0.10 W/m×K 259.11 Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid 0.10 W/m×K 259.32 Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid 0.10 W/m×K 259.52 Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid 0.10 W/m×K 277.52 Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid 0.10 W/m×K 277.74 Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid 0.10 W/m×K 277.93 Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid 0.10 W/m×K 295.67 Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid 0.10 W/m×K 295.90 Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid 0.10 W/m×K 296.10 Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid 0.09 W/m×K 313.79 Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid 0.09 W/m×K 314.02 Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid 0.09 W/m×K 314.22 Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid 0.09 W/m×K 327.69 Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid 0.09 W/m×K 327.93 Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
λliquid 0.09 W/m×K 328.14 Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)

Datasets

  1. Viscosity, Pa*s (2)
  2. Refractive index (Na D-line) (1)
  3. Mass density, kg/m3 (1)
  4. Speed of sound, m/s (2)
  5. Thermal conductivity, W/m/K (2)

Viscosity, Pa*s

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Viscosity, Pa*s - Liquid
293.15 100.00 0.0005
293.15 1000.00 0.0005
293.15 5000.00 0.0005
293.15 10000.00 0.0006
293.15 20000.00 0.0006
293.15 30000.00 0.0007
293.15 40000.00 0.0008
293.15 50000.00 0.0009
293.15 60000.00 0.0010
293.15 70000.00 0.0010
293.15 80000.00 0.0011
293.15 100000.00 0.0013
293.15 120000.00 0.0015
293.15 140000.00 0.0017
298.15 100.00 0.0005
298.15 1000.00 0.0005
298.15 5000.00 0.0005
298.15 10000.00 0.0005
298.15 20000.00 0.0006
298.15 30000.00 0.0007
298.15 40000.00 0.0007
298.15 50000.00 0.0008
298.15 60000.00 0.0009
298.15 70000.00 0.0010
298.15 80000.00 0.0011
298.15 100000.00 0.0012
298.15 120000.00 0.0014
298.15 140000.00 0.0016
313.15 100.00 0.0004
313.15 1000.00 0.0004
313.15 5000.00 0.0004
313.15 10000.00 0.0005
313.15 20000.00 0.0005
313.15 30000.00 0.0006
313.15 40000.00 0.0006
313.15 50000.00 0.0007
313.15 60000.00 0.0008
313.15 70000.00 0.0008
313.15 80000.00 0.0009
313.15 100000.00 0.0010
313.15 120000.00 0.0012
313.15 140000.00 0.0014
323.15 100.00 0.0004
323.15 1000.00 0.0004
323.15 5000.00 0.0004
323.15 10000.00 0.0004
323.15 20000.00 0.0005
323.15 30000.00 0.0005
323.15 40000.00 0.0006
323.15 50000.00 0.0006
323.15 60000.00 0.0007
323.15 70000.00 0.0007
323.15 80000.00 0.0008
323.15 100000.00 0.0009
323.15 120000.00 0.0011
323.15 140000.00 0.0012
333.15 100.00 0.0003
333.15 1000.00 0.0003
333.15 5000.00 0.0004
333.15 10000.00 0.0004
333.15 20000.00 0.0004
333.15 30000.00 0.0005
333.15 40000.00 0.0005
333.15 50000.00 0.0006
333.15 60000.00 0.0006
333.15 70000.00 0.0007
333.15 80000.00 0.0007
333.15 100000.00 0.0008
333.15 120000.00 0.0010
333.15 140000.00 0.0011
348.15 100.00 0.0003
348.15 1000.00 0.0003
348.15 5000.00 0.0003
348.15 10000.00 0.0003
348.15 20000.00 0.0004
348.15 30000.00 0.0004
348.15 40000.00 0.0005
348.15 50000.00 0.0005
348.15 60000.00 0.0005
348.15 70000.00 0.0006
348.15 80000.00 0.0007
348.15 100000.00 0.0008
348.15 120000.00 0.0009
348.15 140000.00 0.0010
353.15 100.00 0.0003
353.15 1000.00 0.0003
353.15 5000.00 0.0003
353.15 10000.00 0.0003
353.15 20000.00 0.0004
353.15 30000.00 0.0004
353.15 40000.00 0.0004
353.15 50000.00 0.0005
353.15 60000.00 0.0005
353.15 70000.00 0.0006
353.15 80000.00 0.0006
353.15 100000.00 0.0007
353.15 120000.00 0.0008
353.15 140000.00 0.0009
Reference
Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Viscosity, Pa*s - Liquid
303.15 101.30 0.0005
Reference

Refractive index (Na D-line)

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Refractive index (Na D-line) - Liquid
298.15 101.33 1.3891
293.15 101.00 1.4211
303.15 101.00 1.416
313.15 101.00 1.4109
323.15 101.00 1.4055
293.15 101.00 1.3916
303.15 101.00 1.3866
313.15 101.00 1.3814
323.15 101.00 1.3763
Reference

Mass density, kg/m3

Fixed Measured
Pressure, kPa - Liquid Temperature, K - Liquid Mass density, kg/m3 - Liquid
100.00 298.15 687.32
Reference

Speed of sound, m/s

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Speed of sound, m/s - Liquid
294.06 100.00 1099.7
304.03 100.00 1058.5
313.81 100.00 1017.3
323.56 100.00 978.2
333.42 100.00 938.5
342.88 100.00 898.0
352.86 100.00 858.9
363.55 100.00 821.9
294.37 3000.00 1127.4
304.16 3000.00 1088.2
313.92 3000.00 1037.2
323.61 3000.00 999.1
333.48 3000.00 968.0
343.07 3000.00 927.9
352.89 3000.00 891.7
363.39 3000.00 852.2
373.04 3000.00 821.1
383.18 3000.00 783.2
393.83 3000.00 742.3
402.16 3000.00 716.5
412.57 3000.00 677.6
423.95 3000.00 636.8
434.51 3000.00 602.6
443.70 3000.00 569.7
452.94 3000.00 538.4
462.54 3000.00 502.1
472.45 3000.00 464.2
483.15 3000.00 423.5
493.12 3000.00 386.4
502.80 3000.00 350.1
512.41 3000.00 311.4
523.31 3000.00 264.5
294.65 6000.00 1147.6
304.23 6000.00 1109.6
313.96 6000.00 1065.2
323.65 6000.00 1027.4
333.50 6000.00 996.0
343.16 6000.00 954.8
352.94 6000.00 921.1
363.49 6000.00 883.5
373.27 6000.00 843.9
383.80 6000.00 813.8
394.00 6000.00 782.2
402.48 6000.00 750.9
412.84 6000.00 719.3
424.32 6000.00 678.1
434.94 6000.00 647.4
444.00 6000.00 619.6
453.22 6000.00 588.3
463.04 6000.00 558.9
472.86 6000.00 530.7
483.63 6000.00 496.7
493.56 6000.00 464.9
503.17 6000.00 435.4
513.04 6000.00 404.0
523.97 6000.00 371.4
294.84 10000.00 1176.1
304.27 10000.00 1136.9
313.82 10000.00 1100.1
323.67 10000.00 1060.4
333.46 10000.00 1028.0
343.22 10000.00 990.3
353.01 10000.00 961.7
363.54 10000.00 925.7
373.41 10000.00 888.2
384.11 10000.00 855.6
394.15 10000.00 825.8
402.64 10000.00 800.2
413.07 10000.00 766.7
424.49 10000.00 732.1
435.26 10000.00 701.0
444.22 10000.00 677.1
454.37 10000.00 648.8
463.43 10000.00 622.7
473.22 10000.00 596.3
484.05 10000.00 569.9
494.09 10000.00 542.2
503.79 10000.00 516.1
513.78 10000.00 491.8
524.59 10000.00 463.0
294.97 12000.00 1181.7
304.27 12000.00 1147.7
313.85 12000.00 1110.8
323.71 12000.00 1075.4
333.40 12000.00 1041.9
343.21 12000.00 1008.5
353.04 12000.00 975.5
363.58 12000.00 943.8
373.49 12000.00 908.6
384.26 12000.00 876.5
394.19 12000.00 848.1
402.78 12000.00 819.5
413.22 12000.00 791.3
424.59 12000.00 756.7
435.36 12000.00 726.5
444.36 12000.00 700.3
455.24 12000.00 671.1
463.72 12000.00 651.6
473.48 12000.00 627.7
484.30 12000.00 598.4
494.42 12000.00 576.5
504.09 12000.00 550.4
514.01 12000.00 526.6
524.70 12000.00 501.3
Reference
Fixed Measured
Pressure, kPa - Liquid Temperature, K - Liquid Speed of sound, m/s - Liquid
100.00 293.15 1104.6
100.00 303.15 1061.7
100.00 313.15 1019.1
100.00 323.15 977.9
100.00 333.15 935.8
100.00 343.15 897.3
100.00 353.15 858.2
100.00 363.15 817.2
100.00 373.15 780.4
10000.00 293.15 1178.5
10000.00 303.15 1139.3
10000.00 313.15 1100.9
10000.00 323.15 1063.5
10000.00 333.15 1026.6
10000.00 343.15 992.6
10000.00 353.15 958.0
10000.00 363.15 924.3
10000.00 373.15 891.0
20000.00 293.15 1244.6
20000.00 303.15 1208.6
20000.00 313.15 1173.0
20000.00 323.15 1138.8
20000.00 333.15 1105.2
20000.00 343.15 1071.6
20000.00 353.15 1041.7
20000.00 363.15 1011.1
20000.00 373.15 980.7
30000.00 293.15 1304.8
30000.00 303.15 1270.2
30000.00 313.15 1237.0
30000.00 323.15 1204.7
30000.00 333.15 1173.0
30000.00 343.15 1142.7
30000.00 353.15 1114.1
30000.00 363.15 1085.5
30000.00 373.15 1057.5
40000.00 293.15 1358.5
40000.00 303.15 1326.8
40000.00 313.15 1295.2
40000.00 323.15 1264.6
40000.00 333.15 1234.2
40000.00 343.15 1205.7
40000.00 353.15 1178.7
40000.00 363.15 1151.4
40000.00 373.15 1125.2
50000.00 293.15 1410.3
50000.00 303.15 1378.5
50000.00 313.15 1349.3
50000.00 323.15 1319.0
50000.00 333.15 1290.2
50000.00 343.15 1262.9
50000.00 353.15 1236.1
50000.00 363.15 1211.3
50000.00 373.15 1185.9
60000.00 293.15 1458.1
60000.00 303.15 1427.0
60000.00 313.15 1397.6
60000.00 323.15 1369.8
60000.00 333.15 1341.8
60000.00 343.15 1315.4
60000.00 353.15 1290.4
60000.00 363.15 1265.7
60000.00 373.15 1242.1
70000.00 293.15 1502.5
70000.00 303.15 1472.6
70000.00 313.15 1443.4
70000.00 323.15 1416.6
70000.00 333.15 1390.0
70000.00 343.15 1363.5
70000.00 353.15 1339.5
70000.00 363.15 1316.6
70000.00 373.15 1293.1
80000.00 293.15 1544.7
80000.00 303.15 1515.6
80000.00 313.15 1487.6
80000.00 323.15 1461.2
80000.00 333.15 1434.9
80000.00 343.15 1410.8
80000.00 353.15 1386.8
80000.00 363.15 1364.4
80000.00 373.15 1341.5
90000.00 293.15 1584.5
90000.00 303.15 1556.4
90000.00 313.15 1529.0
90000.00 323.15 1503.4
90000.00 333.15 1479.0
90000.00 343.15 1453.6
90000.00 353.15 1431.0
90000.00 363.15 1408.2
90000.00 373.15 1386.0
100000.00 293.15 1622.6
100000.00 303.15 1594.5
100000.00 313.15 1568.7
100000.00 323.15 1543.4
100000.00 333.15 1519.0
100000.00 343.15 1495.3
100000.00 353.15 1472.5
100000.00 363.15 1449.9
100000.00 373.15 1428.5
110000.00 293.15 1658.9
110000.00 303.15 1632.1
110000.00 313.15 1605.9
110000.00 323.15 1581.4
110000.00 333.15 1557.7
110000.00 343.15 1534.0
110000.00 353.15 1512.1
110000.00 363.15 1490.6
110000.00 373.15 1469.2
120000.00 293.15 1694.0
120000.00 303.15 1667.5
120000.00 313.15 1641.7
120000.00 323.15 1617.8
120000.00 333.15 1594.1
120000.00 343.15 1571.7
120000.00 353.15 1549.6
120000.00 363.15 1529.0
120000.00 373.15 1508.2
130000.00 293.15 1727.5
130000.00 303.15 1701.6
130000.00 313.15 1676.3
130000.00 323.15 1653.1
130000.00 333.15 1629.5
130000.00 343.15 1607.2
130000.00 353.15 1585.9
130000.00 363.15 1565.5
130000.00 373.15 1545.1
140000.00 293.15 1760.1
140000.00 303.15 1734.3
140000.00 313.15 1709.4
140000.00 323.15 1686.4
140000.00 333.15 1663.5
140000.00 343.15 1641.7
140000.00 353.15 1620.5
140000.00 363.15 1600.8
140000.00 373.15 1580.3
150000.00 293.15 1791.1
150000.00 303.15 1766.4
150000.00 313.15 1741.7
150000.00 323.15 1718.6
150000.00 333.15 1696.2
150000.00 343.15 1675.0
150000.00 353.15 1654.1
150000.00 363.15 1634.2
150000.00 373.15 1614.0
Reference

Thermal conductivity, W/m/K

Fixed Measured
Pressure, kPa - Liquid Temperature, K - Liquid Thermal conductivity, W/m/K - Liquid
77.00 295.00 0.0960
Reference
Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Thermal conductivity, W/m/K - Liquid
254.60 100.00 0.1047
254.51 5000.00 0.1066
254.67 10100.00 0.1088
254.77 20000.00 0.1121
254.73 30000.00 0.1157
274.66 100.00 0.1004
274.63 5000.00 0.1021
274.61 10000.00 0.1041
274.61 20000.00 0.1080
274.57 30000.00 0.1114
295.33 100.00 0.0959
295.22 5000.00 0.0979
295.22 10100.00 0.1003
295.06 20100.00 0.1042
295.04 30100.00 0.1083
314.99 100.00 0.0907
314.85 5000.00 0.0930
314.87 10000.00 0.0953
314.93 20000.00 0.0996
314.91 29900.00 0.1038
334.53 100.00 0.0859
334.49 5100.00 0.0886
334.56 10000.00 0.0908
334.62 20000.00 0.0958
334.59 30000.00 0.0999
354.50 200.00 0.0817
354.78 5100.00 0.0843
354.83 10000.00 0.0868
354.73 20000.00 0.0915
354.80 30000.00 0.0960
374.63 400.00 0.0784
374.61 5000.00 0.0807
374.18 10000.00 0.0830
374.21 19900.00 0.0875
374.25 29900.00 0.0925
Reference

Correlations

Property Value Unit Temperature (K) Source
Cp,gas [130.63; 537.55] 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 A8.46350e+01
Coefficient B-4.70350e+02
Coefficient C6.10324e+00
Coefficient D4.11240e-04
Coefficient E-1.29260e-07
Temperature range, min.200.00
Temperature range, max.1500.00
Cp,gas 130.63 J/mol×K 200.00 Calculated Property
Cp,gas 214.18 J/mol×K 344.44 Calculated Property
Cp,gas 287.25 J/mol×K 488.89 Calculated Property
Cp,gas 346.86 J/mol×K 633.33 Calculated Property
Cp,gas 395.75 J/mol×K 777.78 Calculated Property
Cp,gas 436.25 J/mol×K 922.22 Calculated Property
Cp,gas 469.88 J/mol×K 1066.67 Calculated Property
Cp,gas 497.59 J/mol×K 1211.11 Calculated Property
Cp,gas 520.01 J/mol×K 1355.56 Calculated Property
Cp,gas 537.55 J/mol×K 1500.00 Calculated Property
Property Value Unit Temperature (K) Source
Cp,liquid [183.79; 391.24] J/mol×K [165.78; 520.00] 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 A1.59470e+02
Coefficient B-3.80540e+02
Coefficient C5.46424e+00
Coefficient D-4.42360e-04
Coefficient E3.48870e-06
Temperature range, min.165.78
Temperature range, max.520.00
Cp,liquid 183.79 J/mol×K 165.78 Calculated Property
Cp,liquid 198.54 J/mol×K 205.14 Calculated Property
Cp,liquid 214.52 J/mol×K 244.50 Calculated Property
Cp,liquid 231.65 J/mol×K 283.85 Calculated Property
Cp,liquid 250.24 J/mol×K 323.21 Calculated Property
Cp,liquid 270.85 J/mol×K 362.57 Calculated Property
Cp,liquid 294.20 J/mol×K 401.93 Calculated Property
Cp,liquid 321.22 J/mol×K 441.28 Calculated Property
Cp,liquid 353.08 J/mol×K 480.64 Calculated Property
Cp,liquid 391.24 J/mol×K 520.00 Calculated Property
Property Value Unit Temperature (K) Source
η [0.0086398; 0.0000633] Pa×s [165.78; 543.90] 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-2.22410e+01
Coefficient B1.36560e+03
Coefficient C1.83790e+00
Coefficient D-5.11890e-06
Coefficient E2.00000e+00
Temperature range, min.165.78
Temperature range, max.543.90
η 0.0086398 Pa×s 165.78 Calculated Property
η 0.0022834 Pa×s 207.79 Calculated Property
η 0.0009612 Pa×s 249.81 Calculated Property
η 0.0005182 Pa×s 291.82 Calculated Property
η 0.0003218 Pa×s 333.83 Calculated Property
η 0.0002175 Pa×s 375.85 Calculated Property
η 0.0001546 Pa×s 417.86 Calculated Property
η 0.0001132 Pa×s 459.87 Calculated Property
η 0.0000843 Pa×s 501.89 Calculated Property
η 0.0000633 Pa×s 543.90 Calculated Property
Property Value Unit Temperature (K) Source
ΔvapH [40.71; 1.79] kJ/mol [165.78; 543.80] 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 A4.63300e+01
Coefficient B3.74510e-01
Coefficient C-6.67750e-02
Coefficient D-1.01350e-02
Coefficient E8.08320e-02
Critical temperature, Tc (K)5.43900e+02
Temperature range, min.165.78
Temperature range, max.543.80
ΔvapH 40.71 kJ/mol 165.78 Calculated Property
ΔvapH 39.11 kJ/mol 207.78 Calculated Property
ΔvapH 37.37 kJ/mol 249.78 Calculated Property
ΔvapH 35.45 kJ/mol 291.79 Calculated Property
ΔvapH 33.26 kJ/mol 333.79 Calculated Property
ΔvapH 30.71 kJ/mol 375.79 Calculated Property
ΔvapH 27.62 kJ/mol 417.79 Calculated Property
ΔvapH 23.68 kJ/mol 459.80 Calculated Property
ΔvapH 18.08 kJ/mol 501.80 Calculated Property
ΔvapH 1.79 kJ/mol 543.80 Calculated Property
Property Value Unit Temperature (K) Source
Pvap [1.33; 202.67] kPa [268.57; 398.53] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.40806e+01
Coefficient B-3.12864e+03
Coefficient C-4.17450e+01
Temperature range, min.268.57
Temperature range, max.398.53
Pvap 1.33 kPa 268.57 Calculated Property
Pvap 3.04 kPa 283.01 Calculated Property
Pvap 6.33 kPa 297.45 Calculated Property
Pvap 12.17 kPa 311.89 Calculated Property
Pvap 21.91 kPa 326.33 Calculated Property
Pvap 37.25 kPa 340.77 Calculated Property
Pvap 60.32 kPa 355.21 Calculated Property
Pvap 93.62 kPa 369.65 Calculated Property
Pvap 140.01 kPa 384.09 Calculated Property
Pvap 202.67 kPa 398.53 Calculated Property
Pvap [1.63e-05; 2540.13] kPa [165.78; 543.89] 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 A7.68027e+01
Coefficient B-6.70160e+03
Coefficient C-9.31219e+00
Coefficient D6.80845e-06
Coefficient E2.00000e+00
Temperature range, min.165.78
Temperature range, max.543.89
Pvap 1.63e-05 kPa 165.78 Calculated Property
Pvap 7.83e-03 kPa 207.79 Calculated Property
Pvap 0.36 kPa 249.80 Calculated Property
Pvap 4.76 kPa 291.82 Calculated Property
Pvap 29.28 kPa 333.83 Calculated Property
Pvap 112.16 kPa 375.84 Calculated Property
Pvap 315.13 kPa 417.85 Calculated Property
Pvap 718.46 kPa 459.87 Calculated Property
Pvap 1419.43 kPa 501.88 Calculated Property
Pvap 2540.13 kPa 543.89 Calculated Property
Pvap [1.48e-05; 2584.81] kPa [165.78; 543.96] 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 A8.67458e+01
Coefficient B-7.04177e+03
Coefficient C-1.08858e+01
Coefficient D8.87277e-06
Coefficient E0.00000e+00
Temperature range, min.165.78
Temperature range, max.543.96
Pvap 1.48e-05 kPa 165.78 Calculated Property
Pvap 7.82e-03 kPa 207.80 Calculated Property
Pvap 0.37 kPa 249.82 Calculated Property
Pvap 4.87 kPa 291.84 Calculated Property
Pvap 29.62 kPa 333.86 Calculated Property
Pvap 112.21 kPa 375.88 Calculated Property
Pvap 313.08 kPa 417.90 Calculated Property
Pvap 713.56 kPa 459.92 Calculated Property
Pvap 1420.70 kPa 501.94 Calculated Property
Pvap 2584.81 kPa 543.96 Calculated Property
Pvap [1.50e-03; 6.58] kPa [194.64; 298.44] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.36943e+01
Coefficient B-2.95268e+03
Coefficient C-4.84440e+01
ReferenceMilazzo, 1956, 2
CommentCoefficents calculated by NIST from author's data.
Temperature range, min.194.64
Temperature range, max.298.44
Pvap 1.50e-03 kPa 194.64 Calculated Property
Pvap 6.57e-03 kPa 206.17 Calculated Property
Pvap 0.02 kPa 217.71 Calculated Property
Pvap 0.07 kPa 229.24 Calculated Property
Pvap 0.19 kPa 240.77 Calculated Property
Pvap 0.45 kPa 252.31 Calculated Property
Pvap 0.99 kPa 263.84 Calculated Property
Pvap 1.98 kPa 275.37 Calculated Property
Pvap 3.71 kPa 286.91 Calculated Property
Pvap 6.58 kPa 298.44 Calculated Property
Pvap [6.38; 103.91] kPa [297.51; 373.28] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.36700e+01
Coefficient B-2.89628e+03
Coefficient C-5.24150e+01
ReferenceWilliamham, Taylor, et al., 1945
Temperature range, min.297.51
Temperature range, max.373.28
Pvap 6.38 kPa 297.51 Calculated Property
Pvap 9.44 kPa 305.93 Calculated Property
Pvap 13.63 kPa 314.35 Calculated Property
Pvap 19.24 kPa 322.77 Calculated Property
Pvap 26.59 kPa 331.19 Calculated Property
Pvap 36.05 kPa 339.60 Calculated Property
Pvap 48.05 kPa 348.02 Calculated Property
Pvap 63.03 kPa 356.44 Calculated Property
Pvap 81.47 kPa 364.86 Calculated Property
Pvap 103.91 kPa 373.28 Calculated Property
Pvap [1.50e-03; 6.58] kPa [194.64; 298.44] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.36943e+01
Coefficient B-2.95268e+03
Coefficient C-4.84440e+01
ReferenceMilazzo, 1956
CommentCoefficents calculated by NIST from author's data.
Temperature range, min.194.64
Temperature range, max.298.44
Pvap 1.50e-03 kPa 194.64 Calculated Property
Pvap 6.57e-03 kPa 206.17 Calculated Property
Pvap 0.02 kPa 217.71 Calculated Property
Pvap 0.07 kPa 229.24 Calculated Property
Pvap 0.19 kPa 240.77 Calculated Property
Pvap 0.45 kPa 252.31 Calculated Property
Pvap 0.99 kPa 263.84 Calculated Property
Pvap 1.98 kPa 275.37 Calculated Property
Pvap 3.71 kPa 286.91 Calculated Property
Pvap 6.58 kPa 298.44 Calculated Property
Property Value Unit Temperature (K) Source
ρl [788.61; 242.16] kg/m3 [165.78; 543.89] 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 A5.54271e+01
Coefficient B2.49240e-01
Coefficient C5.43900e+02
Coefficient D2.56020e-01
Temperature range, min.165.78
Temperature range, max.543.89
ρl 788.61 kg/m3 165.78 Calculated Property
ρl 759.50 kg/m3 207.79 Calculated Property
ρl 728.79 kg/m3 249.80 Calculated Property
ρl 696.07 kg/m3 291.82 Calculated Property
ρl 660.78 kg/m3 333.83 Calculated Property
ρl 622.01 kg/m3 375.84 Calculated Property
ρl 578.20 kg/m3 417.85 Calculated Property
ρl 526.22 kg/m3 459.87 Calculated Property
ρl 457.46 kg/m3 501.88 Calculated Property
ρl 242.16 kg/m3 543.89 Calculated Property
Property Value Unit Temperature (K) Source
γ [0.03; 0.01] N/m [165.75; 372.35] 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 A4.48057e-02
Coefficient B-8.88000e-05
Coefficient C0.00000e+00
Coefficient D0.00000e+00
Coefficient E0.00000e+00
Temperature range, min.165.75
Temperature range, max.372.35
γ 0.03 N/m 165.75 Calculated Property
γ 0.03 N/m 188.71 Calculated Property
γ 0.03 N/m 211.66 Calculated Property
γ 0.02 N/m 234.62 Calculated Property
γ 0.02 N/m 257.57 Calculated Property
γ 0.02 N/m 280.53 Calculated Property
γ 0.02 N/m 303.48 Calculated Property
γ 0.02 N/m 326.44 Calculated Property
γ 0.01 N/m 349.39 Calculated Property
γ 0.01 N/m 372.35 Calculated Property
γ [0.03; 1.75e-05] N/m [165.78; 540.78] 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-9.75920e-03
Coefficient B3.19440e+01
Coefficient C-3.31030e+00
Coefficient D3.74400e-04
Coefficient E-5.39940e-06
CommentRange stopped where the equation turns negative; ChemSep gives it to 543.8 K.
Temperature range, min.165.78
Temperature range, max.540.78
γ 0.03 N/m 165.78 Calculated Property
γ 0.03 N/m 207.45 Calculated Property
γ 0.02 N/m 249.11 Calculated Property
γ 0.02 N/m 290.78 Calculated Property
γ 0.02 N/m 332.44 Calculated Property
γ 0.01 N/m 374.11 Calculated Property
γ 0.01 N/m 415.78 Calculated Property
γ 0.01 N/m 457.44 Calculated Property
γ 0.00 N/m 499.11 Calculated Property
γ 1.75e-05 N/m 540.78 Calculated Property
Property Value Unit Temperature (K) Source
λgas [0.00; 0.11] W/m×K [165.78; 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 A1.14010e-05
Coefficient B1.36320e+00
Coefficient C2.86230e+02
Coefficient D6.06520e+03
Temperature range, min.165.78
Temperature range, max.1000.00
λgas 0.00 W/m×K 165.78 Calculated Property
λgas 0.01 W/m×K 258.47 Calculated Property
λgas 0.02 W/m×K 351.16 Calculated Property
λgas 0.03 W/m×K 443.85 Calculated Property
λgas 0.04 W/m×K 536.54 Calculated Property
λgas 0.05 W/m×K 629.23 Calculated Property
λgas 0.06 W/m×K 721.93 Calculated Property
λgas 0.08 W/m×K 814.62 Calculated Property
λgas 0.09 W/m×K 907.31 Calculated Property
λgas 0.11 W/m×K 1000.00 Calculated Property
Property Value Unit Temperature (K) Source
λliquid [0.13; 0.08] W/m×K [165.78; 372.39] 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 A4.47440e-02
Coefficient B-4.24140e+01
Coefficient C-1.73610e+00
Coefficient D-2.32250e-03
Coefficient E-4.05970e-06
Temperature range, min.165.78
Temperature range, max.372.39
λliquid 0.13 W/m×K 165.78 Calculated Property
λliquid 0.12 W/m×K 188.74 Calculated Property
λliquid 0.12 W/m×K 211.69 Calculated Property
λliquid 0.11 W/m×K 234.65 Calculated Property
λliquid 0.11 W/m×K 257.61 Calculated Property
λliquid 0.10 W/m×K 280.56 Calculated Property
λliquid 0.10 W/m×K 303.52 Calculated Property
λliquid 0.09 W/m×K 326.48 Calculated Property
λliquid 0.09 W/m×K 349.43 Calculated Property
λliquid 0.08 W/m×K 372.39 Calculated Property

Similar Compounds

Pentane, 2,4-dimethyl-. Heptane, 2,2,4,6,6-pentamethyl-. Pentane, 2,2-dimethyl-. Hexane, 2,2,5-trimethyl-. Hexane, 2,4,4-trimethyl-. Heptane, 2,2,6-trimethyl-. Nonane, 2,2,4,4,6,8,8-heptamethyl-. 1,1,3,3,5-Pentamethylcyclohexane. Hexane, 2,2,4-trimethyl-. Hexane, 4-ethyl-2,4-dimethyl-. Pentane, 2-methyl-. Hexane, 4-ethyl-2,2-dimethyl-. Heptane, 2,4,4-trimethyl-. Hexane, 2,2,4,5-tetramethyl-. Cyclohexane, 1,1,3,5-tetramethyl-, cis-.

Find more compounds similar to Pentane, 2,2,4-trimethyl-.

Mixtures

Find more mixtures with Pentane, 2,2,4-trimethyl-.

Sources

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