Chemical Properties of 1-Octanol (CAS 111-87-5)

1-Octanol

InChI
InChI=1S/C8H18O/c1-2-3-4-5-6-7-8-9/h9H,2-8H2,1H3
InChI Key
KBPLFHHGFOOTCA-UHFFFAOYSA-N
Formula
C8H18O
SMILES
CCCCCCCCO
Molecular Weight1
130.23
CAS
111-87-5
Other Names
  • 1-Hydroxyoctane
  • 1-Octyl alcohol
  • Alcohol C-8
  • Alfol 8
  • Dytol M-83
  • Emery 3322
  • Emery 3324
  • Epal 8
  • Heptyl carbinol
  • Lorol 20
  • Lorol C 8-98
  • NSC 9823
  • Octanol-(1)
  • Octilin
  • Octyl alcohol, normal-primary
  • Prim-n-octyl alcohol
  • Primary octyl alcohol
  • Sipol L8
  • capryl alcohol
  • caprylic alcohol
  • n-Heptyl carbinol
  • n-Octan-1-ol
  • n-Octanol
  • n-octyl alcohol
  • octan-1-ol
  • octanol
  • octyl alcohol
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Contents

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

Physical Properties

Property Value Unit Source
ω 0.5870 KDB
PAff 799.00 kJ/mol NIST
Δcliquid [-5295.50; -5285.60] kJ/mol Show Hide
Δcliquid -5294.00 ± 0.60 kJ/mol NIST
Δcliquid -5295.50 ± 1.00 kJ/mol NIST
Δcliquid -5285.70 ± 2.70 kJ/mol NIST
Δcliquid -5285.60 kJ/mol NIST
μ 2.00 debye KDB
η [0.0071430; 0.0075080] Pa×s Show Hide
η 0.0075080 Pa×s Study of molecular interactions in binary liquid mixtures of 1-octanol with n-hexane, n-octane, and n-decane using volumetric, viscometric, and acoustic properties
η 0.0071430 Pa×s Volumetric and Viscometric Properties of Binary Liquid Mixtures of Ethylene Glycol Monomethyl Ether + 1-Hexanol, 1-Octanol, and 1-Decanol at Temperatures of T = (293.15, 298.15, 303.15, and 308.15) K
Δf -120.20 kJ/mol KDB
Δfgas [-362.20; -354.10] kJ/mol Show Hide
Δfgas -360.10 kJ/mol KDB
Δfgas -355.50 kJ/mol NIST
Δfgas -355.60 ± 0.70 kJ/mol NIST
Δfgas -356.90 ± 1.30 kJ/mol NIST
Δfgas -354.10 kJ/mol NIST
Δfgas -354.20 ± 1.20 kJ/mol NIST
Δfgas -362.20 ± 3.10 kJ/mol NIST
Δfliquid [-435.00; -425.20] kJ/mol Show Hide
Δfliquid -426.60 ± 0.60 kJ/mol NIST
Δfliquid -428.00 ± 1.10 kJ/mol NIST
Δfliquid -425.20 ± 1.10 kJ/mol NIST
Δfliquid -435.00 ± 2.70 kJ/mol NIST
Δfus [23.70; 25.14] kJ/mol Show Hide
Δfus 25.14 kJ/mol Heat Capacities and Derived Thermodynamic Functions of 1-Hexanol, 1-Heptanol, 1-Octanol, and 1-Decanol between 5 K and 390 K
Δfus 23.70 kJ/mol Measurements, Correlations, and Mod. UNIFAC (Do) Prediction of (Solid-Liquid) Phase Equilibria Diagrams in Binary Systems (Aliphatic Ketone + an Alcohol)
Δsub 100.40 kJ/mol NIST
Δvap 69.84 kJ/mol Relay (1.0) Calculated Property
IE 9.94 eV Relay (1.0) Calculated Property
log10WS [-2.39; -2.39]   Show Hide
log10WS -2.39 Aq. Solubility Prediction
log10WS -2.39 Estimated Solubility
logPoct/wat 2.339 Crippen Calculated Property
McVol 129.450 ml/mol McGowan Calculated Property
NFPA Fire 2 KDB
NFPA Health 1 KDB
Pc 2777.00 kPa KDB
ρc [256.55; 265.66] kg/m3 Show Hide
ρc 261.76 ± 3.91 kg/m3 NIST
ρc 265.66 kg/m3 NIST
ρc 256.55 ± 6.51 kg/m3 NIST
ρc 265.66 ± 2.60 kg/m3 NIST
Inp [175.63; 1095.00]   Show Hide
Inp 1051.43 NIST
Inp 1051.79 NIST
Inp 1052.54 NIST
Inp 1052.35 NIST
Inp 1060.90 NIST
Inp 1060.50 NIST
Inp 1059.90 NIST
Inp 1059.70 NIST
Inp 1060.90 NIST
Inp 1060.50 NIST
Inp 1059.90 NIST
Inp 1059.70 NIST
Inp 1052.99 NIST
Inp 1055.41 NIST
Inp 1053.90 NIST
Inp 1034.80 NIST
Inp 1042.30 NIST
Inp 1051.70 NIST
Inp 1082.00 NIST
Inp 1051.00 NIST
Inp 1052.00 NIST
Inp 1053.00 NIST
Inp 1053.00 NIST
Inp 1053.00 NIST
Inp 1054.00 NIST
Inp 1054.00 NIST
Inp 1054.00 NIST
Inp 1055.00 NIST
Inp 1057.00 NIST
Inp 1060.00 NIST
Inp 1061.00 NIST
Inp 1066.00 NIST
Inp 1049.00 NIST
Inp 1050.00 NIST
Inp 1049.00 NIST
Inp 1042.00 NIST
Inp 1057.00 NIST
Inp 1060.00 NIST
Inp 1058.00 NIST
Inp 1044.00 NIST
Inp 1064.00 NIST
Inp 1058.00 NIST
Inp 1060.00 NIST
Inp 1042.00 NIST
Inp 1061.00 NIST
Inp 1057.00 NIST
Inp 1073.00 NIST
Inp 1059.00 NIST
Inp 1059.00 NIST
Inp 1068.00 NIST
Inp 1071.00 NIST
Inp 1062.00 NIST
Inp 1053.00 NIST
Inp 1060.00 NIST
Inp 1078.00 NIST
Inp 1078.00 NIST
Inp 1060.00 NIST
Inp 1053.00 NIST
Inp 1060.00 NIST
Inp 1059.00 NIST
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Inp 1063.00 NIST
Inp 1061.00 NIST
Inp 1062.00 NIST
Inp 1067.00 NIST
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Inp 1061.00 NIST
Inp 1063.00 NIST
Inp 1055.00 NIST
Inp 1060.00 NIST
Inp 1065.00 NIST
Inp 1061.00 NIST
Inp 1059.00 NIST
Inp 1061.00 NIST
Inp 1070.00 NIST
Inp 1061.00 NIST
Inp 1093.00 NIST
Inp 1093.00 NIST
Inp 1071.00 NIST
Inp 1074.00 NIST
Inp 1064.00 NIST
Inp 1082.00 NIST
Inp 1054.00 NIST
Inp 1070.00 NIST
Inp 1076.00 NIST
Inp 1069.00 NIST
Inp 1079.00 NIST
Inp 1074.00 NIST
Inp 1070.00 NIST
Inp 1068.00 NIST
Inp 1052.00 NIST
Inp 1073.00 NIST
Inp 1065.00 NIST
Inp 1076.00 NIST
Inp 1070.60 NIST
Inp 1072.00 NIST
Inp 1068.00 NIST
Inp 1074.00 NIST
Inp 1084.00 NIST
Inp 1050.00 NIST
Inp 1068.00 NIST
Inp 1065.00 NIST
Inp 1070.00 NIST
Inp 1064.00 NIST
Inp 1063.00 NIST
Inp 1066.90 NIST
Inp 1066.90 NIST
Inp 1066.50 NIST
Inp 1075.00 NIST
Inp 1070.00 NIST
Inp 1070.00 NIST
Inp 1071.00 NIST
Inp 1068.00 NIST
Inp 1072.00 NIST
Inp 1057.00 NIST
Inp 1074.00 NIST
Inp 1073.00 NIST
Inp 1054.00 NIST
Inp 1068.00 NIST
Inp 1053.20 NIST
Inp 1080.00 NIST
Inp 1071.00 NIST
Inp 1068.70 NIST
Inp 1051.00 NIST
Inp 1064.00 NIST
Inp 1073.00 NIST
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Inp 1072.00 NIST
Inp 1070.00 NIST
Inp 1054.00 NIST
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Inp 1070.00 NIST
Inp 1065.00 NIST
Inp 1065.00 NIST
Inp 1064.00 NIST
Inp 1065.00 NIST
Inp 1067.00 NIST
Inp 1056.00 NIST
Inp 1055.40 NIST
Inp 1067.00 NIST
Inp 1054.00 NIST
Inp 1052.00 NIST
Inp 1080.00 NIST
Inp 1068.00 NIST
Inp 1061.00 NIST
Inp 1070.00 NIST
Inp 1072.00 NIST
Inp 1061.70 NIST
Inp 1061.70 NIST
Inp 1069.00 NIST
Inp 1069.00 NIST
Inp 1071.00 NIST
Inp 1071.00 NIST
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Inp 1051.00 NIST
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Inp 1083.00 NIST
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Inp 1071.00 NIST
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Inp 1072.00 NIST
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Inp 1076.00 NIST
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Inp 1060.00 NIST
Inp 1057.00 NIST
Inp 1084.00 NIST
Inp 1070.00 NIST
Inp 1080.10 NIST
Inp 1068.00 NIST
Inp 1068.00 NIST
Inp 1080.00 NIST
Inp 1068.00 NIST
Inp 1072.00 NIST
Inp 1051.00 NIST
Inp 1070.00 NIST
Inp 1070.00 NIST
Inp 1074.00 NIST
Inp 1074.00 NIST
Inp 1052.00 NIST
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Inp 1081.00 NIST
Inp 1070.00 NIST
Inp 1059.00 NIST
Inp 1052.00 NIST
Inp 1054.00 NIST
Inp 1054.00 NIST
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Inp 1051.00 NIST
Inp 1051.00 NIST
Inp 1053.00 NIST
Inp 1071.00 NIST
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Inp 1057.00 NIST
Inp 1071.00 NIST
Inp 1072.00 NIST
Inp 1078.00 NIST
Inp 1095.00 NIST
Inp 1069.00 NIST
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Inp 1073.00 NIST
Inp 1076.00 NIST
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Inp 1089.00 NIST
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Inp 1048.00 NIST
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Inp 1070.00 NIST
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Inp 1039.00 NIST
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Inp 1091.00 NIST
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Inp 1070.00 NIST
Inp 1067.00 NIST
Inp 1067.00 NIST
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Inp 1061.00 NIST
Inp 1052.00 NIST
Inp 1070.00 NIST
Inp 1069.00 NIST
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Inp 1048.00 NIST
Inp 1073.00 NIST
Inp 1052.00 NIST
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Inp 1050.00 NIST
Inp 1076.00 NIST
Inp 1053.00 NIST
Inp 1053.00 NIST
Inp 1056.80 NIST
Inp 1056.00 NIST
Inp 1074.00 NIST
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Inp 1072.00 NIST
Inp 1038.00 NIST
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Inp 1069.00 NIST
Inp 1070.00 NIST
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Inp 1070.00 NIST
Inp 1055.00 NIST
Inp 1064.00 NIST
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Inp 1070.00 NIST
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Inp 1075.00 NIST
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Inp 1061.00 NIST
Inp 1069.70 NIST
Inp 1075.00 NIST
Inp 1077.00 NIST
Inp 1087.00 NIST
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Inp 1056.00 NIST
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Inp 1084.00 NIST
Inp 1053.00 NIST
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Inp 1059.00 NIST
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Inp Outlier 175.63 NIST
Inp Outlier 177.62 NIST
Inp Outlier 176.31 NIST
Inp 1084.00 NIST
Inp 1080.00 NIST
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Inp 1081.00 NIST
I [1507.00; 1605.00]   Show Hide
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I 1564.00 NIST
I 1562.00 NIST
I 1566.00 NIST
I 1565.00 NIST
I 1568.00 NIST
I 1559.00 NIST
I 1540.00 NIST
I 1548.00 NIST
I Outlier 1605.00 NIST
I 1561.00 NIST
I 1574.00 NIST
I 1543.00 NIST
I 1562.00 NIST
I 1557.00 NIST
I 1563.00 NIST
I 1562.00 NIST
I 1562.00 NIST
I 1562.00 NIST
I 1550.00 NIST
I 1562.00 NIST
I 1536.00 NIST
I 1538.00 NIST
I 1539.00 NIST
I 1562.00 NIST
I 1562.00 NIST
I 1562.00 NIST
I 1562.00 NIST
I 1551.00 NIST
I 1549.00 NIST
I 1562.00 NIST
I 1562.00 NIST
I 1567.00 NIST
I Outlier 1519.00 NIST
I 1556.00 NIST
I 1562.00 NIST
I 1562.00 NIST
I 1562.00 NIST
I 1562.00 NIST
I 1562.00 NIST
I 1549.00 NIST
I Outlier 1519.00 NIST
I 1562.00 NIST
I 1562.00 NIST
I 1562.00 NIST
I 1562.00 NIST
I 1562.00 NIST
I 1562.00 NIST
I 1548.00 NIST
I 1568.00 NIST
I Outlier 1519.00 NIST
I 1553.00 NIST
I Outlier 1507.00 NIST
I 1554.00 NIST
I 1573.00 NIST
I 1573.00 NIST
I 1557.00 NIST
I 1557.00 NIST
I Outlier 1519.00 NIST
I Outlier 1513.00 NIST
I 1546.00 NIST
I 1557.00 NIST
I 1558.00 NIST
I Outlier 1520.00 NIST
I 1559.00 NIST
I 1566.00 NIST
I 1544.00 NIST
I 1538.00 NIST
I 1549.00 NIST
I 1555.00 NIST
I 1573.00 NIST
I 1565.00 NIST
I 1562.00 NIST
I 1567.00 NIST
Tboil [451.65; 469.20] K Show Hide
Tboil 468.20 K Ternary phase diagrams for aqueous mixtures of butyric acid with several solvents: experimental and correlated data
Tboil 466.00 K The role of organic diluents in the aspects of equilibrium, kinetics and thermodynamic model for silver ion extraction using an extractant D2EHPA
Tboil 468.00 K (Liquid + liquid) equilibria of (water + propionic acid + alcohol) ternary systems
Tboil 468.00 K (Liquid + liquid) equilibria of (water + lactic acid + alcohol) ternary systems
Tboil 468.31 K KDB
Tboil 467.85 ± 0.60 K NIST
Tboil 469.20 K NIST
Tboil 467.60 K NIST
Tboil 468.35 ± 0.50 K NIST
Tboil 468.15 ± 1.00 K NIST
Tboil 468.00 ± 2.00 K NIST
Tboil 468.15 ± 1.00 K NIST
Tboil 468.15 ± 1.00 K NIST
Tboil 467.35 ± 1.00 K NIST
Tboil 468.15 ± 0.50 K NIST
Tboil 468.15 ± 2.00 K NIST
Tboil 466.35 ± 1.00 K NIST
Tboil 467.65 ± 1.00 K NIST
Tboil 467.75 ± 1.00 K NIST
Tboil 468.15 ± 2.00 K NIST
Tboil 468.43 ± 0.20 K NIST
Tboil 469.15 ± 2.00 K NIST
Tboil 467.65 ± 1.00 K NIST
Tboil 468.35 ± 0.25 K NIST
Tboil 468.15 ± 3.90 K NIST
Tboil 467.65 ± 2.00 K NIST
Tboil 468.15 ± 2.00 K NIST
Tboil 467.65 ± 0.40 K NIST
Tboil 467.85 ± 0.50 K NIST
Tboil 467.60 ± 0.50 K NIST
Tboil 469.15 ± 3.00 K NIST
Tboil 468.30 ± 0.30 K NIST
Tboil 468.30 ± 0.50 K NIST
Tboil 468.30 ± 0.50 K NIST
Tboil 468.30 ± 1.00 K NIST
Tboil 467.20 ± 0.40 K NIST
Tboil 468.15 ± 2.00 K NIST
Tboil Outlier 452.65 ± 3.00 K NIST
Tboil 468.65 ± 1.00 K NIST
Tboil 469.05 ± 1.00 K NIST
Tboil 467.30 ± 2.00 K NIST
Tboil Outlier 451.65 ± 1.50 K NIST
Tboil 468.40 ± 3.00 K NIST
Tboil 468.65 ± 3.00 K NIST
Tboil 468.65 ± 1.00 K NIST
Tboil 464.15 ± 3.00 K NIST
Tc [650.56; 668.00] K Show Hide
Tc 652.50 K KDB
Tc 652.50 ± 0.50 K NIST
Tc 652.20 ± 0.80 K NIST
Tc 652.40 ± 0.60 K NIST
Tc 652.40 ± 0.60 K NIST
Tc 652.60 K NIST
Tc 650.56 ± 0.30 K NIST
Tc 652.50 K NIST
Tc Outlier 668.00 ± 2.00 K NIST
Tc 657.80 K NIST
Tc 658.60 K NIST
Tfus [257.60; 259.15] K Show Hide
Tfus 257.70 K SLE and LLE for tri-butylphosphate or tri-octylamine contained systems; extractive solvents of Molybdenum
Tfus 258.20 K Phase equilibria of didecyldimethylammonium nitrate ionic liquid with water and organic solvents
Tfus 258.03 K Experimental (Solid + Liquid) and (Liquid + Liquid) Equilibria and Excess Molar Volume of Alkanol + Acetonitrile, Propanenitrile, and Butanenitrile Mixtures
Tfus Outlier 259.15 K Phase Equilibria Study of the Binary Systems (N-Butyl-4-methylpyridinium Tosylate Ionic Liquid + Organic Solvent, or Water)
Tfus 257.85 K Solid-Liquid Equilibria, Excess Molar Volumes, and Molar Refractivity Deviations for Extractive Solvents of Molybdenum
Tfus 257.60 K KDB
Tfus 257.65 K Aq. Solubility Prediction
Vc [0.497; 0.497] m3/kmol Show Hide
Vc 0.497 m3/kmol KDB
Vc 0.497 m3/kmol NIST
Zc 0.2543990 KDB

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,gas [290.08; 353.18] J/mol×K [474.62; 634.38] Show Hide
Cp,gas 290.08 J/mol×K 474.62 Joback Calculated Property
Cp,gas 301.62 J/mol×K 501.25 Joback Calculated Property
Cp,gas 312.74 J/mol×K 527.87 Joback Calculated Property
Cp,gas 323.45 J/mol×K 554.50 Joback Calculated Property
Cp,gas 333.75 J/mol×K 581.13 Joback Calculated Property
Cp,gas 343.66 J/mol×K 607.75 Joback Calculated Property
Cp,gas 353.18 J/mol×K 634.38 Joback Calculated Property
Cp,liquid [284.50; 379.00] J/mol×K [286.00; 313.15] Show Hide
Cp,liquid 284.50 J/mol×K 286.00 NIST
Cp,liquid 312.10 J/mol×K 298.00 NIST
Cp,liquid 324.30 J/mol×K 298.00 NIST
Cp,liquid 304.00 J/mol×K 298.15 Volumetric Properties, Viscosities, and Isobaric Heat Capacities of Imidazolium Octanoate Protic Ionic Liquid in Molecular Solvents
Cp,liquid 304.00 J/mol×K 298.15 NIST
Cp,liquid 305.55 J/mol×K 298.15 NIST
Cp,liquid 329.00 J/mol×K 303.15 Volumetric Properties, Viscosities, and Isobaric Heat Capacities of Imidazolium Octanoate Protic Ionic Liquid in Molecular Solvents
Cp,liquid 329.50 J/mol×K 303.20 NIST
Cp,liquid 354.00 J/mol×K 308.15 Volumetric Properties, Viscosities, and Isobaric Heat Capacities of Imidazolium Octanoate Protic Ionic Liquid in Molecular Solvents
Cp,liquid 318.30 J/mol×K 310.67 NIST
Cp,liquid 379.00 J/mol×K 313.15 Volumetric Properties, Viscosities, and Isobaric Heat Capacities of Imidazolium Octanoate Protic Ionic Liquid in Molecular Solvents
η [0.0017820; 0.0134930] Pa×s [283.15; 348.15] Show Hide
η 0.0134930 Pa×s 283.15 Density and Viscosity of the Binary Systems Ethanol + Butan-1-ol, + Pentan-1-ol, + Heptan-1-ol, + Octan-1-ol, Nonan-1-ol, + Decan-1-ol at 0.1 MPa and Temperatures from 283.15 K to 313.15 K
η 0.0134930 Pa×s 283.15 Measurement of Density and Viscosity of Binary 1-Alkanol Systems (C8-C11) at 101 kPa and Temperatures from (283.15 to 313.15) K
η 0.0110700 Pa×s 288.15 Densities and Viscosities of Four Binary Diethyl Carbonate + 1-Alcohol Systems from (288.15 to 313.15) K
η 0.0108720 Pa×s 288.15 Measurement of Density and Viscosity of Binary 1-Alkanol Systems (C8-C11) at 101 kPa and Temperatures from (283.15 to 313.15) K
η 0.0091610 Pa×s 293.15 Densities and Viscosities of Four Binary Diethyl Carbonate + 1-Alcohol Systems from (288.15 to 313.15) K
η 0.0089440 Pa×s 293.15 Measurement of Density and Viscosity of Binary 1-Alkanol Systems (C8-C11) at 101 kPa and Temperatures from (283.15 to 313.15) K
η 0.0090160 Pa×s 293.15 Density and Viscosity of the Binary Systems Ethanol + Butan-1-ol, + Pentan-1-ol, + Heptan-1-ol, + Octan-1-ol, Nonan-1-ol, + Decan-1-ol at 0.1 MPa and Temperatures from 283.15 K to 313.15 K
η 0.0074980 Pa×s 298.15 Measurement of Density and Viscosity of Binary 1-Alkanol Systems (C8-C11) at 101 kPa and Temperatures from (283.15 to 313.15) K
η 0.0073980 Pa×s 298.15 Density and Viscosity of Binary Mixtures of {1-Butyl-3-methylimidazolium Thiocyanate + 1-Heptanol, 1-Octanol, 1-Nonanol, or 1-Decanol}
η 0.0076880 Pa×s 298.15 Densities and Viscosities of Four Binary Diethyl Carbonate + 1-Alcohol Systems from (288.15 to 313.15) K
η 0.0073900 Pa×s 298.15 Density and Viscosity of the Binary Systems Ethanol + Butan-1-ol, + Pentan-1-ol, + Heptan-1-ol, + Octan-1-ol, Nonan-1-ol, + Decan-1-ol at 0.1 MPa and Temperatures from 283.15 K to 313.15 K
η 0.0076610 Pa×s 298.15 Acoustical and Excess Properties of {Chlorobenzene + 1-Hexanol, or 1-Heptanol, or 1-Octanol, or 1-Nonanol, or 1-Decanol} at (298.15, 303.15, 308.15, and 313.15) K
η 0.0073650 Pa×s 298.15 Density, Viscosity, and Speed of Sound of (1-Octanol + 2-Methoxyethanol), (1-Octanol + N,N-Dimethylacetamide), and (1-Octanol + Acetophenone) at Temperatures of (298.15, 308.15, and 318.15) K
η 0.0062730 Pa×s 303.15 Measurement of Density and Viscosity of Binary 1-Alkanol Systems (C8-C11) at 101 kPa and Temperatures from (283.15 to 313.15) K
η 0.0064040 Pa×s 303.15 Densities and Viscosities of Four Binary Diethyl Carbonate + 1-Alcohol Systems from (288.15 to 313.15) K
η 0.0064020 Pa×s 303.15 Acoustical and Excess Properties of {Chlorobenzene + 1-Hexanol, or 1-Heptanol, or 1-Octanol, or 1-Nonanol, or 1-Decanol} at (298.15, 303.15, 308.15, and 313.15) K
η 0.0064330 Pa×s 303.15 Densities, Viscosities, and Speed of Sound Studies of Binary Mixtures of Methylbenzene with Heptan-1-ol, Octan-1-ol, and Decan-1-ol at (303.15 and 313.15) K
η 0.0064460 Pa×s 303.15 Densities, Viscosities, and Ultrasonic Velocity Studies of Binary Mixtures of Chloroform with Octan-1-ol and Decan-1-ol at (303.15 and 313.15) K
η 0.0063060 Pa×s 303.15 Density and Viscosity of the Binary Systems Ethanol + Butan-1-ol, + Pentan-1-ol, + Heptan-1-ol, + Octan-1-ol, Nonan-1-ol, + Decan-1-ol at 0.1 MPa and Temperatures from 283.15 K to 313.15 K
η 0.0052510 Pa×s 308.15 Density, Viscosity, and Speed of Sound of (1-Octanol + 2-Methoxyethanol), (1-Octanol + N,N-Dimethylacetamide), and (1-Octanol + Acetophenone) at Temperatures of (298.15, 308.15, and 318.15) K
η 0.0052850 Pa×s 308.15 Density and Viscosity of Binary Mixtures of {1-Butyl-3-methylimidazolium Thiocyanate + 1-Heptanol, 1-Octanol, 1-Nonanol, or 1-Decanol}
η 0.0053420 Pa×s 308.15 Measurement of Density and Viscosity of Binary 1-Alkanol Systems (C8-C11) at 101 kPa and Temperatures from (283.15 to 313.15) K
η 0.0054250 Pa×s 308.15 Acoustical and Excess Properties of {Chlorobenzene + 1-Hexanol, or 1-Heptanol, or 1-Octanol, or 1-Nonanol, or 1-Decanol} at (298.15, 303.15, 308.15, and 313.15) K
η 0.0046200 Pa×s 313.15 Densities and Viscosities of Four Binary Diethyl Carbonate + 1-Alcohol Systems from (288.15 to 313.15) K
η 0.0046030 Pa×s 313.15 Densities, Viscosities, and Speed of Sound Studies of Binary Mixtures of Methylbenzene with Heptan-1-ol, Octan-1-ol, and Decan-1-ol at (303.15 and 313.15) K
η 0.0046040 Pa×s 313.15 Densities, Viscosities, and Ultrasonic Velocity Studies of Binary Mixtures of Chloroform with Octan-1-ol and Decan-1-ol at (303.15 and 313.15) K
η 0.0045400 Pa×s 313.15 Measurement of Density and Viscosity of Binary 1-Alkanol Systems (C8-C11) at 101 kPa and Temperatures from (283.15 to 313.15) K
η 0.0045870 Pa×s 313.15 Density and Viscosity of the Binary Systems Ethanol + Butan-1-ol, + Pentan-1-ol, + Heptan-1-ol, + Octan-1-ol, Nonan-1-ol, + Decan-1-ol at 0.1 MPa and Temperatures from 283.15 K to 313.15 K
η 0.0046280 Pa×s 313.15 Acoustical and Excess Properties of {Chlorobenzene + 1-Hexanol, or 1-Heptanol, or 1-Octanol, or 1-Nonanol, or 1-Decanol} at (298.15, 303.15, 308.15, and 313.15) K
η 0.0038650 Pa×s 318.15 Density, Viscosity, and Speed of Sound of (1-Octanol + 2-Methoxyethanol), (1-Octanol + N,N-Dimethylacetamide), and (1-Octanol + Acetophenone) at Temperatures of (298.15, 308.15, and 318.15) K
η 0.0038870 Pa×s 318.15 Density and Viscosity of Binary Mixtures of {1-Butyl-3-methylimidazolium Thiocyanate + 1-Heptanol, 1-Octanol, 1-Nonanol, or 1-Decanol}
η 0.0029310 Pa×s 328.15 Density and Viscosity of Binary Mixtures of {1-Butyl-3-methylimidazolium Thiocyanate + 1-Heptanol, 1-Octanol, 1-Nonanol, or 1-Decanol}
η 0.0022620 Pa×s 338.15 Density and Viscosity of Binary Mixtures of {1-Butyl-3-methylimidazolium Thiocyanate + 1-Heptanol, 1-Octanol, 1-Nonanol, or 1-Decanol}
η 0.0017820 Pa×s 348.15 Density and Viscosity of Binary Mixtures of {1-Butyl-3-methylimidazolium Thiocyanate + 1-Heptanol, 1-Octanol, 1-Nonanol, or 1-Decanol}
εr 9.85 298.15 Comparative Dielectric Study and Molecular Interactions of Binary Mixtures of (Cyclohexanone + 1-Alkanols) and (Cyclopentanone or Cyclohexanone + Cyclohexanol or Cyclohexane) at T = 298.15 K
ΔfusH 25.24 kJ/mol 258.40 NIST
ΔvapH [47.80; 70.40] kJ/mol [267.00; 515.00] Show Hide
ΔvapH 64.00 ± 1.00 kJ/mol 267.00 NIST
ΔvapH 64.00 kJ/mol 274.50 NIST
ΔvapH 69.60 kJ/mol 301.50 NIST
ΔvapH 68.70 kJ/mol 318.00 NIST
ΔvapH 70.40 kJ/mol 323.00 NIST
ΔvapH 67.30 kJ/mol 364.00 NIST
ΔvapH 61.60 kJ/mol 396.00 NIST
ΔvapH 67.50 kJ/mol 405.50 NIST
ΔvapH 65.00 kJ/mol 410.00 NIST
ΔvapH 56.60 kJ/mol 438.00 NIST
ΔvapH 52.50 kJ/mol 452.00 NIST
ΔvapH 50.63 kJ/mol 468.30 KDB
ΔvapH 47.80 kJ/mol 515.00 NIST
Pvap [1.00e-03; 101.40] kPa [288.15; 468.47] Show Hide
Pvap 1.00e-03 kPa 288.15 Vapor Liquid Equilibrium between (278.15 and 323.15) K and Excess Functions at T ) 298.15 K for 1-Bromobutane with 1-Octanol or 1-Decanol
Pvap 3.00e-03 kPa 293.15 Vapor Liquid Equilibrium between (278.15 and 323.15) K and Excess Functions at T ) 298.15 K for 1-Bromobutane with 1-Octanol or 1-Decanol
Pvap 3.00e-03 kPa 293.15 Isothermal (vapour + liquid) equilibrium at several temperatures of (1-chlorobutane + 1-octanol, or 1-decanol)
Pvap 0.01 kPa 298.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 7.00e-03 kPa 298.15 Vapor Liquid Equilibrium between (278.15 and 323.15) K and Excess Functions at T ) 298.15 K for 1-Bromobutane with 1-Octanol or 1-Decanol
Pvap 7.00e-03 kPa 298.15 Isothermal (vapour + liquid) equilibrium at several temperatures of (1-chlorobutane + 1-octanol, or 1-decanol)
Pvap 0.01 kPa 303.15 Isothermal (vapour + liquid) equilibrium at several temperatures of (1-chlorobutane + 1-octanol, or 1-decanol)
Pvap 0.01 kPa 303.15 Vapor Liquid Equilibrium between (278.15 and 323.15) K and Excess Functions at T ) 298.15 K for 1-Bromobutane with 1-Octanol or 1-Decanol
Pvap 0.02 kPa 303.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 0.02 kPa 308.15 Isothermal (vapour + liquid) equilibrium at several temperatures of (1-chlorobutane + 1-octanol, or 1-decanol)
Pvap 0.02 kPa 308.15 Vapor Liquid Equilibrium between (278.15 and 323.15) K and Excess Functions at T ) 298.15 K for 1-Bromobutane with 1-Octanol or 1-Decanol
Pvap 0.03 kPa 308.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 0.03 kPa 313.15 Vapor Liquid Equilibrium between (278.15 and 323.15) K and Excess Functions at T ) 298.15 K for 1-Bromobutane with 1-Octanol or 1-Decanol
Pvap 0.04 kPa 313.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 0.03 kPa 313.15 Isothermal (vapour + liquid) equilibrium at several temperatures of (1-chlorobutane + 1-octanol, or 1-decanol)
Pvap 0.05 kPa 318.15 Vapor Liquid Equilibrium between (278.15 and 323.15) K and Excess Functions at T ) 298.15 K for 1-Bromobutane with 1-Octanol or 1-Decanol
Pvap 0.06 kPa 318.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 0.05 kPa 318.15 Isothermal (vapour + liquid) equilibrium at several temperatures of (1-chlorobutane + 1-octanol, or 1-decanol)
Pvap 0.06 kPa 319.82 Thermogravimetric measurement of evaporation: Data analysis based on the Stefan tube
Pvap 0.08 kPa 323.15 Vapor Liquid Equilibrium between (278.15 and 323.15) K and Excess Functions at T ) 298.15 K for 1-Bromobutane with 1-Octanol or 1-Decanol
Pvap 0.09 kPa 323.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 0.08 kPa 323.15 Isothermal (vapour + liquid) equilibrium at several temperatures of (1-chlorobutane + 1-octanol, or 1-decanol)
Pvap 0.09 kPa 324.46 Thermogravimetric measurement of evaporation: Data analysis based on the Stefan tube
Pvap 0.14 kPa 328.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 0.20 kPa 333.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 0.22 kPa 333.69 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 0.21 kPa 333.93 Thermogravimetric measurement of evaporation: Data analysis based on the Stefan tube
Pvap 0.22 kPa 333.97 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 0.24 kPa 334.46 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 0.29 kPa 338.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 0.20 kPa 338.55 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 0.39 kPa 341.76 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 0.39 kPa 342.10 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 0.41 kPa 343.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 0.38 kPa 343.23 Thermogravimetric measurement of evaporation: Data analysis based on the Stefan tube
Pvap 0.37 kPa 343.33 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 0.40 kPa 343.39 Thermogravimetric measurement of evaporation: Data analysis based on the Stefan tube
Pvap 0.39 kPa 344.50 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 0.57 kPa 348.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 0.54 kPa 348.15 Thermogravimetric measurement of evaporation: Data analysis based on the Stefan tube
Pvap 0.57 kPa 348.20 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 0.59 kPa 348.72 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 0.60 kPa 349.10 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 0.59 kPa 349.38 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 0.75 kPa 352.09 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 0.80 kPa 352.98 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 0.79 kPa 353.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 0.81 kPa 353.96 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 0.85 kPa 354.85 Vapor Pressure and Isobaric Vapor-Liquid Equilibrium for Binary Systems of Furfural, 2-Acetylfuran, and 5-Methylfurfural at 3.60 and 5.18 kPa
Pvap 0.79 kPa 354.96 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 1.07 kPa 357.90 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 1.06 kPa 357.94 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 1.06 kPa 357.99 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 1.07 kPa 358.15 Vapor Pressure and Isobaric Vapor-Liquid Equilibrium for Binary Systems of Furfural, 2-Acetylfuran, and 5-Methylfurfural at 3.60 and 5.18 kPa
Pvap 1.07 kPa 358.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 1.07 kPa 358.41 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 1.36 kPa 362.32 Thermogravimetric measurement of evaporation: Data analysis based on the Stefan tube
Pvap 1.43 kPa 362.88 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 1.45 kPa 363.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 1.45 kPa 363.30 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 1.46 kPa 363.51 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 1.51 kPa 363.55 Vapor Pressure and Isobaric Vapor-Liquid Equilibrium for Binary Systems of Furfural, 2-Acetylfuran, and 5-Methylfurfural at 3.60 and 5.18 kPa
Pvap 1.47 kPa 364.35 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 1.93 kPa 368.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 2.01 kPa 368.25 Vapor Pressure and Isobaric Vapor-Liquid Equilibrium for Binary Systems of Furfural, 2-Acetylfuran, and 5-Methylfurfural at 3.60 and 5.18 kPa
Pvap 2.10 kPa 369.69 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 2.09 kPa 369.76 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 2.13 kPa 369.90 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 2.13 kPa 370.00 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 2.54 kPa 373.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 2.99 kPa 376.05 Vapor Pressure and Isobaric Vapor-Liquid Equilibrium for Binary Systems of Furfural, 2-Acetylfuran, and 5-Methylfurfural at 3.60 and 5.18 kPa
Pvap 3.32 kPa 378.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 3.44 kPa 379.04 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 3.49 kPa 379.35 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 3.49 kPa 379.45 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 3.49 kPa 379.49 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 4.01 kPa 381.75 Vapor Pressure and Isobaric Vapor-Liquid Equilibrium for Binary Systems of Furfural, 2-Acetylfuran, and 5-Methylfurfural at 3.60 and 5.18 kPa
Pvap 4.29 kPa 383.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 5.01 kPa 386.05 Vapor Pressure and Isobaric Vapor-Liquid Equilibrium for Binary Systems of Furfural, 2-Acetylfuran, and 5-Methylfurfural at 3.60 and 5.18 kPa
Pvap 5.17 kPa 387.20 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 5.16 kPa 387.28 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 5.18 kPa 387.87 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 5.17 kPa 387.92 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 5.48 kPa 388.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 6.01 kPa 389.95 Vapor Pressure and Isobaric Vapor-Liquid Equilibrium for Binary Systems of Furfural, 2-Acetylfuran, and 5-Methylfurfural at 3.60 and 5.18 kPa
Pvap 6.14 kPa 390.95 Thermogravimetric measurement of evaporation: Data analysis based on the Stefan tube
Pvap 6.94 kPa 393.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 7.01 kPa 393.15 Vapor Pressure and Isobaric Vapor-Liquid Equilibrium for Binary Systems of Furfural, 2-Acetylfuran, and 5-Methylfurfural at 3.60 and 5.18 kPa
Pvap 8.02 kPa 396.05 Vapor Pressure and Isobaric Vapor-Liquid Equilibrium for Binary Systems of Furfural, 2-Acetylfuran, and 5-Methylfurfural at 3.60 and 5.18 kPa
Pvap 8.36 kPa 397.32 Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 8.71 kPa 398.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 9.02 kPa 398.55 Vapor Pressure and Isobaric Vapor-Liquid Equilibrium for Binary Systems of Furfural, 2-Acetylfuran, and 5-Methylfurfural at 3.60 and 5.18 kPa
Pvap 9.99 kPa 400.95 Vapor Pressure and Isobaric Vapor-Liquid Equilibrium for Binary Systems of Furfural, 2-Acetylfuran, and 5-Methylfurfural at 3.60 and 5.18 kPa
Pvap 10.83 kPa 403.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 11.10 kPa 403.71 Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 13.57 kPa 407.24 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 13.36 kPa 408.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 13.58 kPa 408.44 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 13.55 kPa 408.90 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 13.95 kPa 409.14 Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 13.55 kPa 409.30 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 14.97 kPa 410.15 Vapor Pressure and Isobaric Vapor-Liquid Equilibrium for Binary Systems of Furfural, 2-Acetylfuran, and 5-Methylfurfural at 3.60 and 5.18 kPa
Pvap 16.36 kPa 413.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 16.83 kPa 413.79 Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 19.91 kPa 417.35 Vapor Pressure and Isobaric Vapor-Liquid Equilibrium for Binary Systems of Furfural, 2-Acetylfuran, and 5-Methylfurfural at 3.60 and 5.18 kPa
Pvap 20.50 kPa 417.83 Isobaric vapor-liquid equilibrium for binary systems containing benzothiophene
Pvap 19.88 kPa 418.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 20.33 kPa 418.61 Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 20.33 kPa 418.62 Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 20.33 kPa 418.63 Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 23.99 kPa 423.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 24.62 kPa 423.70 Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 28.76 kPa 428.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 30.40 kPa 428.60 Isobaric vapor-liquid equilibrium for binary systems containing benzothiophene
Pvap 29.45 kPa 428.65 Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 34.27 kPa 433.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 34.89 kPa 433.49 Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 40.47 kPa 435.48 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 40.00 kPa 436.67 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 41.50 kPa 437.35 Isobaric vapor-liquid equilibrium for binary systems containing benzothiophene
Pvap 40.08 kPa 437.67 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 40.83 kPa 438.12 Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 40.83 kPa 438.14 Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 40.61 kPa 438.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 40.53 kPa 438.31 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 40.53 kPa 438.58 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 40.53 kPa 438.80 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 47.73 kPa 442.88 Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 47.88 kPa 443.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 48.62 kPa 443.61 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 50.50 kPa 443.90 Isobaric vapor-liquid equilibrium for binary systems containing benzothiophene
Pvap 52.15 kPa 445.86 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 56.17 kPa 448.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 60.70 kPa 449.55 Isobaric vapor-liquid equilibrium for binary systems containing benzothiophene
Pvap 60.37 kPa 450.34 Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 60.03 kPa 450.45 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 65.45 kPa 453.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 67.60 kPa 454.35 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 71.00 kPa 454.52 Isobaric vapor-liquid equilibrium for binary systems containing benzothiophene
Pvap 74.25 kPa 457.08 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 74.88 kPa 457.52 Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 75.95 kPa 458.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 81.00 kPa 459.23 Isobaric vapor-liquid equilibrium for binary systems containing benzothiophene
Pvap 81.52 kPa 460.31 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 87.73 kPa 463.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 91.10 kPa 463.21 Isobaric vapor-liquid equilibrium for binary systems containing benzothiophene
Pvap 89.16 kPa 463.50 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 93.42 kPa 465.25 Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 93.54 kPa 465.29 Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 100.30 kPa 466.61 Isobaric vapor-liquid equilibrium for binary systems containing benzothiophene
Pvap 97.64 kPa 466.80 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 101.40 kPa 468.15 Vapor pressure of 1-octanol below 5 kPa using DSC
Pvap 101.40 kPa 468.47 Vapor pressure of 1-octanol below 5 kPa using DSC
n0 [1.41800; 1.42980]   [293.15; 318.20] Show Hide
n0 1.42910 293.15 Experimental solubility for betulin and estrone in various solvents within the temperature range T = (293.2 to 328.2) K
n0 1.42930 293.15 Experimental study and ERAS modeling of the excess molar enthalpy of (acetonitrile + 1-heptanol or 1-octanol) mixtures at (298.15, 313.15, and 323.15) K and atmospheric pressure
n0 1.42958 293.15 Excess molar volumes and viscosities of (1,1,2,2-tetrabromoethane + 1-alkanols) at T = (293.15 and 303.15) K
n0 1.42941 293.15 Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrachloroethane and 1-alkanols binary mixtures
n0 1.42900 293.15 Effect of temperature and chain length on the viscosity and surface tension of binary systems of N,N-dimethylformamide with 1-octanol, 1-nonanol and 1-decanol
n0 1.42958 293.15 Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrabromoethane and 1-alkanols binary mixtures
n0 1.42980 293.15 Densities, Excess Molar Volumes, and Isobaric Thermal Expansibilities for 1,2-Ethanediol + 1-Butanol, or 1-Hexanol, or 1-Octanol in the Temperature Range from (293.15 to 313.15) K
n0 1.42695 298.15 Liquid Liquid Phase Equilibria of 1-Propanol + Water + n-Alcohol Ternary Systems at 298.15 K and Atmospheric Pressure
n0 1.42740 298.15 Density, Surface Tension, and Refractive Index of Octane + 1-Alkanol Mixtures at T ) 298.15 K.
n0 1.42884 298.15 Atmospheric densities and interfacial tensions for 1- alkanol (1-butanol to 1-octanol) + water and ether (MTBE, ETBE, DIPE, TAME and THP) + water demixed mixtures.
n0 1.42750 298.15 Effect of Pressure on the Static Relative Permittivities of Alkan-1-ols at 298.15 K
n0 1.42800 298.15 Densities, Excess Molar Volumes, and Isobaric Thermal Expansibilities for 1,2-Ethanediol + 1-Butanol, or 1-Hexanol, or 1-Octanol in the Temperature Range from (293.15 to 313.15) K
n0 1.42760 298.15 Permittivities, Refractive Indices, Densities, and Excess Properties for Binary Systems Containing 1-Alkanols and Cyclopentanone
n0 1.42700 298.20 Ternary equilibrium data of mixtures consisting of 2-butanol, water, and heavy alcohols at T = 298.2 K
n0 1.42760 298.20 A thermodynamic study of solute solvent interactions through dielectric properties of the mixtures consisting of 1,4-butanediol, 1-octanol, and 1,4-dioxane at different temperatures
n0 1.42700 298.20 Tie-line data for the aqueous solutions of phenol with organic solvents at T = 298.2 K
n0 1.42760 298.20 Solubility and tie line data for the aqueous solutions of butyric acid with 1-octanol and 2-ethyl-1-hexanol at various temperatures
n0 1.42562 303.15 Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrabromoethane and 1-alkanols binary mixtures
n0 1.42563 303.15 Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrachloroethane and 1-alkanols binary mixtures
n0 1.42280 308.20 A thermodynamic study of solute solvent interactions through dielectric properties of the mixtures consisting of 1,4-butanediol, 1-octanol, and 1,4-dioxane at different temperatures
n0 1.41800 318.20 A thermodynamic study of solute solvent interactions through dielectric properties of the mixtures consisting of 1,4-butanediol, 1-octanol, and 1,4-dioxane at different temperatures
n0 1.41850 318.20 A thermodynamic study of solute solvent interactions through dielectric properties of the mixtures consisting of 1,4-butanediol, 1-octanol, and 1,4-dioxane at different temperatures
ρl [774.43; 832.13] kg/m3 [283.15; 363.15] Show Hide
ρl 832.13 kg/m3 283.15 Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
ρl 832.11 kg/m3 283.15 Densities and Viscosities of Three Binary Monoglyme + 1-Alcohol Systems from (283.15 to 313.15) K
ρl 832.06 kg/m3 283.15 Excess molar volumes of binary mixtures of 1,3-dimethylimidazolidin-2-one with an alkan-1-ol at the temperatures 283.15 K, 298.15 K, and 313.15 K
ρl 832.07 kg/m3 283.15 Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl 828.71 kg/m3 288.15 Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
ρl 828.66 kg/m3 288.15 Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl 826.00 kg/m3 293.00 KDB
ρl 824.90 kg/m3 293.15 Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl 825.13 kg/m3 293.15 Densities and Viscosities of Three Binary Monoglyme + 1-Alcohol Systems from (283.15 to 313.15) K
ρl 825.09 kg/m3 293.15 Volume effects for binary mixtures of propane-1,2-diol with methanol, propan-1-ol, hexan-1-ol, octan-1-ol, or nonan-1-ol at temperatures (293.15 to 318.15) K
ρl 825.24 kg/m3 293.15 Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl 824.60 kg/m3 293.15 Densities, Viscosities, and Refractive Indices of Dimethyl Carbonate + 1-Hexanol/1-Octanol Binary Mixtures at Different Temperatures
ρl 824.90 kg/m3 293.15 Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl 825.57 kg/m3 293.15 Isobaric phase equilibrium of morpholine + 1-decanol, volumetric properties and molar refractivity from 293.15 to 333.15 K of morpholine + 1-decanol and 1-octanol + toluene system with applications of Prigogine-Flory-Patterson theory
ρl 831.00 kg/m3 293.15 Interfacial Properties, Densities, and Contact Angles of Task Specific Ionic Liquids
ρl 825.10 kg/m3 293.15 A thermodynamic study of sublimation, dissolution and distribution processes of anti-inflammatory drug Clonixin
ρl 825.27 kg/m3 293.15 Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
ρl 825.05 kg/m3 293.15 Speeds of Sound, Densities, Isobaric Thermal Expansion, Compressibilities, and Internal Pressures of Heptan-1-ol, Octan-1-ol, Nonan-1-ol, and Decan-1-ol at Temperatures from (293 to 318) K and Pressures up to 100 MPa
ρl 825.95 kg/m3 293.20 Modeling extraction equilibria of butyric acid distributed between water and tri-n-butyl amine/diluent or tri-n-butyl phosphate/diluent system: Extension of the LSER approach
ρl 823.60 kg/m3 293.20 Ternary and Quaternary Liquid-Liquid Equilibria for Systems of Methyl Butyl Ketone + Water + Hydroquinone + Phenol at 313.2 K and Atmospheric Pressure
ρl 821.64 kg/m3 298.15 Speeds of Sound, Densities, Isobaric Thermal Expansion, Compressibilities, and Internal Pressures of Heptan-1-ol, Octan-1-ol, Nonan-1-ol, and Decan-1-ol at Temperatures from (293 to 318) K and Pressures up to 100 MPa
ρl 821.84 kg/m3 298.15 Densities, speeds of sound and viscosities of binary mixtures of tetrahydrofuran with 1-hexanol, 1-octanol and 1-decanol at T = (298.15 to 313.15) K
ρl 821.40 kg/m3 298.15 Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl 821.80 kg/m3 298.15 Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl 822.11 kg/m3 298.15 Partial molar volumes of some drug and pro-drug substances in 1-octanol at T = 298.15 K
ρl 821.67 kg/m3 298.15 Excess molar enthalpies of binary systems containing 2-octanone, hexanoic acid, or octanoic acid at T = 298.15 K
ρl 821.79 kg/m3 298.15 Studies of thermophysical properties of binary liquid mixtures of amine and alcohols at various temperatures
ρl 821.22 kg/m3 298.15 Physico-chemical properties of binary mixtures of N,N-dimethylformamide with 1-octanol, 1-nonanol and 1-decanol at different temperatures
ρl 821.81 kg/m3 298.15 Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
ρl 821.65 kg/m3 298.15 Volume effects for binary mixtures of propane-1,2-diol with methanol, propan-1-ol, hexan-1-ol, octan-1-ol, or nonan-1-ol at temperatures (293.15 to 318.15) K
ρl 821.65 kg/m3 298.15 Densities and Excess Molar Volumes of N-Methylmorpholine + 1-Alkanol Systems at 298.15 K
ρl 821.60 kg/m3 298.15 Thermodynamics of 1,3-dimethylurea in eight alcohols
ρl 821.72 kg/m3 298.15 Speeds of Sound and Isentropic Compressibilities in Binary Mixtures of 2-Propanol with Several 1-Alkanols at 298.15K
ρl 821.72 kg/m3 298.15 Thermodynamics of mixtures containing amines. XVI. CE pm of 1-butanol, 1-octanol or 1-decanol + benzylamine systems at (298.15, 308.15, 318.15 and 333.15) K
ρl 821.88 kg/m3 298.15 Thermodynamic, transport and excess properties of 2-butoxy ethanol +1-alkanol (C6,C8,C10) at different temperatures
ρl 823.27 kg/m3 298.15 Phase behaviour of ionic liquid 1-butyl-1-methylpyrrolidinium tris(pentafluoroethyl)trifluorophosphate with alcohols, water and aromatic hydrocarbons
ρl 821.74 kg/m3 298.15 Volumetric and compressibility studies on tri-n-butyl phosphate (TBP)-phase modifier (1-octanol, 1-decanol and isodecanol) interactions from T = (298.15 to 323.15) K
ρl 821.72 kg/m3 298.15 Excess molar volumes of binary mixtures of 1,3-dimethylimidazolidin-2-one with an alkan-1-ol at the temperatures 283.15 K, 298.15 K, and 313.15 K
ρl 821.87 kg/m3 298.15 Effect of chain length of alcohol on thermodynamic properties of their binary mixtures with benzylalcohol
ρl 820.70 kg/m3 298.15 Densities, Viscosities, and Refractive Indices of Dimethyl Carbonate + 1-Hexanol/1-Octanol Binary Mixtures at Different Temperatures
ρl 821.60 kg/m3 298.15 Determination and prediction of solubilities of active pharmaceutical ingredients in selected organic solvents
ρl 821.69 kg/m3 298.15 Density and Relative Permittivity for 1-Alkanols + Dodecane at 298.15 K
ρl 821.63 kg/m3 298.15 Densities and Viscosities of Three Binary Monoglyme + 1-Alcohol Systems from (283.15 to 313.15) K
ρl 822.99 kg/m3 298.15 The physicochemical properties and solubility of pharmaceuticals - Methyl xanthines
ρl 822.28 kg/m3 298.15 Thermodynamics of mixing for binary mixtures of 1-octanol and 1-decanol with n-dodecane and ternary mixture of (TBP + 1-octanol + dodecane) at T = (298.15 to 323.15) K
ρl 822.47 kg/m3 298.15 Excess molar enthalpy of 1-alkanol + 1-octene mixtures at 298.15K Experimental results and theoretical description by means of the ERAS and TB models
ρl 821.40 kg/m3 298.15 Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl 822.21 kg/m3 298.15 Experimental Solid + Liquid Equilibria and Excess Molar Volume of Alkanol + Octylamine Mixtures. Analysis in Terms of ERAS, DISQUAC, and Modified UNIFAC
ρl 821.90 kg/m3 298.15 Isobaric phase equilibrium of morpholine + 1-decanol, volumetric properties and molar refractivity from 293.15 to 333.15 K of morpholine + 1-decanol and 1-octanol + toluene system with applications of Prigogine-Flory-Patterson theory
ρl 821.70 kg/m3 298.15 Viscosities and Densities of Fatty Alcohol Mixtures from 298.15 to 338.15 K: Estimation by Kay's Rule and Prediction by the UNIFAC-VISCO and GC-UNIMOD Group Contribution Methods
ρl 823.27 kg/m3 298.15 Phase behaviour of tricyanomethanide-based ionic liquids with alcohols and hydrocarbons
ρl 821.70 kg/m3 298.15 A thermodynamic study of sublimation, dissolution and distribution processes of anti-inflammatory drug Clonixin
ρl 821.69 kg/m3 298.20 Temperature and concentration dependence of the relative permittivity of (1,3-butanediol + 1-octanol or 1,4-dioxane) binary liquid mixtures
ρl 821.70 kg/m3 298.20 Physical Behavior of the Phases from the Liquid-Liquid Equilibrium of Citrus Essential Oils Systems at 298.2 K
ρl 818.26 kg/m3 303.15 Volumetric and compressibility studies on tri-n-butyl phosphate (TBP)-phase modifier (1-octanol, 1-decanol and isodecanol) interactions from T = (298.15 to 323.15) K
ρl 817.90 kg/m3 303.15 Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl 817.52 kg/m3 303.15 Volumetric and transport properties of ternary mixtures containing 1-alkanol + ethyl ethanoate + cyclohexane at 303.15 K: Experimental data, correlation and prediction by ERAS model
ρl 818.35 kg/m3 303.15 Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl 818.27 kg/m3 303.15 Effect of chain length of alcohol on thermodynamic properties of their binary mixtures with benzylalcohol
ρl 818.33 kg/m3 303.15 Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
ρl 817.90 kg/m3 303.15 Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl 818.18 kg/m3 303.15 Volume effects for binary mixtures of propane-1,2-diol with methanol, propan-1-ol, hexan-1-ol, octan-1-ol, or nonan-1-ol at temperatures (293.15 to 318.15) K
ρl 818.30 kg/m3 303.15 A thermodynamic study of sublimation, dissolution and distribution processes of anti-inflammatory drug Clonixin
ρl 818.14 kg/m3 303.15 Densities and Viscosities of Three Binary Monoglyme + 1-Alcohol Systems from (283.15 to 313.15) K
ρl 818.08 kg/m3 303.15 Isobaric phase equilibrium of morpholine + 1-decanol, volumetric properties and molar refractivity from 293.15 to 333.15 K of morpholine + 1-decanol and 1-octanol + toluene system with applications of Prigogine-Flory-Patterson theory
ρl 817.20 kg/m3 303.15 Densities, Viscosities, and Refractive Indices of Dimethyl Carbonate + 1-Hexanol/1-Octanol Binary Mixtures at Different Temperatures
ρl 818.30 kg/m3 303.15 Effect of polarity and temperature on the binary interaction between D2EHPA extractant and organic solvents (kerosene, n-heptane, chlorobenzene and 1-octanol): Experimental and thermodynamics
ρl 818.79 kg/m3 303.15 Thermodynamics of mixing for binary mixtures of 1-octanol and 1-decanol with n-dodecane and ternary mixture of (TBP + 1-octanol + dodecane) at T = (298.15 to 323.15) K
ρl 818.24 kg/m3 303.15 Excess molar enthalpies and heat capacities of dimethyl sulfoxide + seven normal alkanols at 303.15K and atmospheric pressure
ρl 818.17 kg/m3 303.15 Speeds of Sound, Densities, Isobaric Thermal Expansion, Compressibilities, and Internal Pressures of Heptan-1-ol, Octan-1-ol, Nonan-1-ol, and Decan-1-ol at Temperatures from (293 to 318) K and Pressures up to 100 MPa
ρl 814.67 kg/m3 308.15 Speeds of Sound, Densities, Isobaric Thermal Expansion, Compressibilities, and Internal Pressures of Heptan-1-ol, Octan-1-ol, Nonan-1-ol, and Decan-1-ol at Temperatures from (293 to 318) K and Pressures up to 100 MPa
ρl 814.60 kg/m3 308.15 Viscosities and Densities of Fatty Alcohol Mixtures from 298.15 to 338.15 K: Estimation by Kay's Rule and Prediction by the UNIFAC-VISCO and GC-UNIMOD Group Contribution Methods
ρl 814.31 kg/m3 308.15 Isobaric phase equilibrium of morpholine + 1-decanol, volumetric properties and molar refractivity from 293.15 to 333.15 K of morpholine + 1-decanol and 1-octanol + toluene system with applications of Prigogine-Flory-Patterson theory
ρl 813.80 kg/m3 308.15 Densities, Viscosities, and Refractive Indices of Dimethyl Carbonate + 1-Hexanol/1-Octanol Binary Mixtures at Different Temperatures
ρl 814.76 kg/m3 308.15 Volumetric and compressibility studies on tri-n-butyl phosphate (TBP)-phase modifier (1-octanol, 1-decanol and isodecanol) interactions from T = (298.15 to 323.15) K
ρl 814.40 kg/m3 308.15 Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl 815.27 kg/m3 308.15 Thermodynamics of mixing for binary mixtures of 1-octanol and 1-decanol with n-dodecane and ternary mixture of (TBP + 1-octanol + dodecane) at T = (298.15 to 323.15) K
ρl 814.69 kg/m3 308.15 Volume effects for binary mixtures of propane-1,2-diol with methanol, propan-1-ol, hexan-1-ol, octan-1-ol, or nonan-1-ol at temperatures (293.15 to 318.15) K
ρl 814.80 kg/m3 308.15 A thermodynamic study of sublimation, dissolution and distribution processes of anti-inflammatory drug Clonixin
ρl 814.84 kg/m3 308.15 Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
ρl 814.68 kg/m3 308.15 Effect of chain length of alcohol on thermodynamic properties of their binary mixtures with benzylalcohol
ρl 814.87 kg/m3 308.15 Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl 814.40 kg/m3 308.15 Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl 811.17 kg/m3 313.15 Speeds of Sound, Densities, Isobaric Thermal Expansion, Compressibilities, and Internal Pressures of Heptan-1-ol, Octan-1-ol, Nonan-1-ol, and Decan-1-ol at Temperatures from (293 to 318) K and Pressures up to 100 MPa
ρl 811.17 kg/m3 313.15 Volume effects for binary mixtures of propane-1,2-diol with methanol, propan-1-ol, hexan-1-ol, octan-1-ol, or nonan-1-ol at temperatures (293.15 to 318.15) K
ρl 811.24 kg/m3 313.15 Volumetric and compressibility studies on tri-n-butyl phosphate (TBP)-phase modifier (1-octanol, 1-decanol and isodecanol) interactions from T = (298.15 to 323.15) K
ρl 811.31 kg/m3 313.15 Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
ρl 811.15 kg/m3 313.15 Densities and Viscosities of Three Binary Monoglyme + 1-Alcohol Systems from (283.15 to 313.15) K
ρl 811.20 kg/m3 313.15 Effect of polarity and temperature on the binary interaction between D2EHPA extractant and organic solvents (kerosene, n-heptane, chlorobenzene and 1-octanol): Experimental and thermodynamics
ρl 810.60 kg/m3 313.15 Densities, Viscosities, and Refractive Indices of Dimethyl Carbonate + 1-Hexanol/1-Octanol Binary Mixtures at Different Temperatures
ρl 811.21 kg/m3 313.15 Excess molar volumes of binary mixtures of 1,3-dimethylimidazolidin-2-one with an alkan-1-ol at the temperatures 283.15 K, 298.15 K, and 313.15 K
ρl 810.90 kg/m3 313.15 Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl 811.38 kg/m3 313.15 Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl 811.73 kg/m3 313.15 Thermodynamics of mixing for binary mixtures of 1-octanol and 1-decanol with n-dodecane and ternary mixture of (TBP + 1-octanol + dodecane) at T = (298.15 to 323.15) K
ρl 810.90 kg/m3 313.15 Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl 811.40 kg/m3 313.15 A thermodynamic study of sublimation, dissolution and distribution processes of anti-inflammatory drug Clonixin
ρl 811.04 kg/m3 313.15 Effect of chain length of alcohol on thermodynamic properties of their binary mixtures with benzylalcohol
ρl 811.09 kg/m3 313.15 Isobaric phase equilibrium of morpholine + 1-decanol, volumetric properties and molar refractivity from 293.15 to 333.15 K of morpholine + 1-decanol and 1-octanol + toluene system with applications of Prigogine-Flory-Patterson theory
ρl 807.65 kg/m3 318.15 Speeds of Sound, Densities, Isobaric Thermal Expansion, Compressibilities, and Internal Pressures of Heptan-1-ol, Octan-1-ol, Nonan-1-ol, and Decan-1-ol at Temperatures from (293 to 318) K and Pressures up to 100 MPa
ρl 807.69 kg/m3 318.15 Volumetric and compressibility studies on tri-n-butyl phosphate (TBP)-phase modifier (1-octanol, 1-decanol and isodecanol) interactions from T = (298.15 to 323.15) K
ρl 807.30 kg/m3 318.15 Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl 807.50 kg/m3 318.15 Viscosities and Densities of Fatty Alcohol Mixtures from 298.15 to 338.15 K: Estimation by Kay's Rule and Prediction by the UNIFAC-VISCO and GC-UNIMOD Group Contribution Methods
ρl 807.30 kg/m3 318.15 Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl 807.63 kg/m3 318.15 Volume effects for binary mixtures of propane-1,2-diol with methanol, propan-1-ol, hexan-1-ol, octan-1-ol, or nonan-1-ol at temperatures (293.15 to 318.15) K
ρl 807.70 kg/m3 318.15 Isobaric phase equilibrium of morpholine + 1-decanol, volumetric properties and molar refractivity from 293.15 to 333.15 K of morpholine + 1-decanol and 1-octanol + toluene system with applications of Prigogine-Flory-Patterson theory
ρl 806.90 kg/m3 318.15 Densities, Viscosities, and Refractive Indices of Dimethyl Carbonate + 1-Hexanol/1-Octanol Binary Mixtures at Different Temperatures
ρl 808.17 kg/m3 318.15 Thermodynamics of mixing for binary mixtures of 1-octanol and 1-decanol with n-dodecane and ternary mixture of (TBP + 1-octanol + dodecane) at T = (298.15 to 323.15) K
ρl 807.85 kg/m3 318.15 Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl 807.76 kg/m3 318.15 Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
ρl 803.90 kg/m3 323.15 Densities, Viscosities, and Refractive Indices of Dimethyl Carbonate + 1-Hexanol/1-Octanol Binary Mixtures at Different Temperatures
ρl 804.05 kg/m3 323.15 Isobaric phase equilibrium of morpholine + 1-decanol, volumetric properties and molar refractivity from 293.15 to 333.15 K of morpholine + 1-decanol and 1-octanol + toluene system with applications of Prigogine-Flory-Patterson theory
ρl 804.58 kg/m3 323.15 Thermodynamics of mixing for binary mixtures of 1-octanol and 1-decanol with n-dodecane and ternary mixture of (TBP + 1-octanol + dodecane) at T = (298.15 to 323.15) K
ρl 804.20 kg/m3 323.15 Effect of polarity and temperature on the binary interaction between D2EHPA extractant and organic solvents (kerosene, n-heptane, chlorobenzene and 1-octanol): Experimental and thermodynamics
ρl 804.19 kg/m3 323.15 Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
ρl 804.29 kg/m3 323.15 Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl 803.70 kg/m3 323.15 Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl 803.70 kg/m3 323.15 Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl 804.12 kg/m3 323.15 Volumetric and compressibility studies on tri-n-butyl phosphate (TBP)-phase modifier (1-octanol, 1-decanol and isodecanol) interactions from T = (298.15 to 323.15) K
ρl 800.40 kg/m3 328.15 Viscosities and Densities of Fatty Alcohol Mixtures from 298.15 to 338.15 K: Estimation by Kay's Rule and Prediction by the UNIFAC-VISCO and GC-UNIMOD Group Contribution Methods
ρl 800.58 kg/m3 328.15 Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
ρl 800.70 kg/m3 328.15 Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl 796.93 kg/m3 333.15 Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
ρl 796.88 kg/m3 333.15 Isobaric phase equilibrium of morpholine + 1-decanol, volumetric properties and molar refractivity from 293.15 to 333.15 K of morpholine + 1-decanol and 1-octanol + toluene system with applications of Prigogine-Flory-Patterson theory
ρl 796.90 kg/m3 333.15 Effect of polarity and temperature on the binary interaction between D2EHPA extractant and organic solvents (kerosene, n-heptane, chlorobenzene and 1-octanol): Experimental and thermodynamics
ρl 797.08 kg/m3 333.15 Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl 793.10 kg/m3 338.15 Viscosities and Densities of Fatty Alcohol Mixtures from 298.15 to 338.15 K: Estimation by Kay's Rule and Prediction by the UNIFAC-VISCO and GC-UNIMOD Group Contribution Methods
ρl 793.41 kg/m3 338.15 Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl 789.70 kg/m3 343.15 Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl 785.95 kg/m3 348.15 Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl 782.16 kg/m3 353.15 Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl 778.31 kg/m3 358.15 Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
ρl 774.43 kg/m3 363.15 Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
csound,fluid [1282.90; 1390.20] m/s [288.15; 318.15] Show Hide
csound,fluid 1390.20 m/s 288.15 Ultrasonic study of molecular interactions in binary mixtures of methyl acrylate with 1-alkanols (C4 to C10) at temperatures from (288.15 to 318.15) K
csound,fluid 1364.08 m/s 293.15 Thermodynamic and spectral studies of molecular interactions in binary liquid mixtures of 1-butoxy-2- propanol with 1-alcohols
csound,fluid 1371.50 m/s 293.15 Ultrasonic study of molecular interactions in binary mixtures of methyl acrylate with 1-alkanols (C4 to C10) at temperatures from (288.15 to 318.15) K
csound,fluid 1364.29 m/s 293.15 Thermodynamics of (1-alkanol + linear monoether) systems
csound,fluid 1347.08 m/s 298.15 Thermodynamics of (1-alkanol + linear monoether) systems
csound,fluid 1347.40 m/s 298.15 Micellar Properties and Related Thermodynamic Parameters of Aqueous Anionic Surfactants in the Presence of Monohydric Alcohols
csound,fluid 1352.40 m/s 298.15 Ultrasonic study of molecular interactions in binary mixtures of methyl acrylate with 1-alkanols (C4 to C10) at temperatures from (288.15 to 318.15) K
csound,fluid 1347.32 m/s 298.15 Thermodynamic and spectral studies of molecular interactions in binary liquid mixtures of 1-butoxy-2- propanol with 1-alcohols
csound,fluid 1330.99 m/s 303.15 Thermodynamic and spectral studies of molecular interactions in binary liquid mixtures of 1-butoxy-2- propanol with 1-alcohols
csound,fluid 1333.10 m/s 303.15 Ultrasonic study of molecular interactions in binary mixtures of methyl acrylate with 1-alkanols (C4 to C10) at temperatures from (288.15 to 318.15) K
csound,fluid 1330.20 m/s 303.15 Thermodynamics of (1-alkanol + linear monoether) systems
csound,fluid 1330.58 m/s 303.15 Micellar Properties and Related Thermodynamic Parameters of Aqueous Anionic Surfactants in the Presence of Monohydric Alcohols
csound,fluid 1315.70 m/s 308.15 Ultrasonic study of molecular interactions in binary mixtures of methyl acrylate with 1-alkanols (C4 to C10) at temperatures from (288.15 to 318.15) K
csound,fluid 1314.28 m/s 308.15 Thermodynamic and spectral studies of molecular interactions in binary liquid mixtures of 1-butoxy-2- propanol with 1-alcohols
csound,fluid 1313.92 m/s 308.15 Micellar Properties and Related Thermodynamic Parameters of Aqueous Anionic Surfactants in the Presence of Monohydric Alcohols
csound,fluid 1298.90 m/s 313.15 Ultrasonic study of molecular interactions in binary mixtures of methyl acrylate with 1-alkanols (C4 to C10) at temperatures from (288.15 to 318.15) K
csound,fluid 1297.72 m/s 313.15 Thermodynamic and spectral studies of molecular interactions in binary liquid mixtures of 1-butoxy-2- propanol with 1-alcohols
csound,fluid 1282.90 m/s 318.15 Ultrasonic study of molecular interactions in binary mixtures of methyl acrylate with 1-alkanols (C4 to C10) at temperatures from (288.15 to 318.15) K
γ [0.03; 0.03] N/m [288.15; 308.15] Show Hide
γ 0.03 N/m 288.15 Density and Surface Tension Variation with Temperature for Heptane + 1-Alkanol
γ 0.03 N/m 293.15 Density and Surface Tension Variation with Temperature for Heptane + 1-Alkanol
γ 0.03 N/m 293.20 KDB
γ 0.03 N/m 298.15 Density and Surface Tension Variation with Temperature for Heptane + 1-Alkanol
γ 0.03 N/m 303.15 Density and Surface Tension Variation with Temperature for Heptane + 1-Alkanol
γ 0.03 N/m 308.15 Density and Surface Tension Variation with Temperature for Heptane + 1-Alkanol

Pressure Dependent Properties

Property Value Unit Pressure (kPa) Source
Tboilr 371.20 K 2.50 NIST

Datasets

  1. Isobaric coefficient of expansion, 1/K (1)
  2. Mass density, kg/m3 (5)
  3. Thermal conductivity, W/m/K (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 0.0008
278.15 10000.00 0.0008
278.15 15000.00 0.0008
278.15 20000.00 0.0008
278.15 25000.00 0.0007
278.15 30000.00 0.0007
278.15 35000.00 0.0007
278.15 40000.00 0.0007
278.15 45000.00 0.0007
278.15 50000.00 0.0007
278.15 55000.00 0.0007
288.15 5000.00 0.0008
288.15 10000.00 0.0008
288.15 15000.00 0.0008
288.15 20000.00 0.0008
288.15 25000.00 0.0007
288.15 30000.00 0.0007
288.15 35000.00 0.0007
288.15 40000.00 0.0007
288.15 45000.00 0.0007
288.15 50000.00 0.0007
288.15 55000.00 0.0007
298.15 5000.00 0.0008
298.15 10000.00 0.0008
298.15 15000.00 0.0008
298.15 20000.00 0.0008
298.15 25000.00 0.0007
298.15 30000.00 0.0007
298.15 35000.00 0.0007
298.15 40000.00 0.0007
298.15 45000.00 0.0007
298.15 50000.00 0.0007
298.15 55000.00 0.0007
308.15 5000.00 0.0008
308.15 10000.00 0.0008
308.15 15000.00 0.0008
308.15 20000.00 0.0008
308.15 25000.00 0.0008
308.15 30000.00 0.0007
308.15 35000.00 0.0007
308.15 40000.00 0.0007
308.15 45000.00 0.0007
308.15 50000.00 0.0007
308.15 55000.00 0.0007
318.15 5000.00 0.0009
318.15 10000.00 0.0008
318.15 15000.00 0.0008
318.15 20000.00 0.0008
318.15 25000.00 0.0008
318.15 30000.00 0.0008
318.15 35000.00 0.0007
318.15 40000.00 0.0007
318.15 45000.00 0.0007
318.15 50000.00 0.0007
318.15 55000.00 0.0007
328.15 5000.00 0.0009
328.15 10000.00 0.0008
328.15 15000.00 0.0008
328.15 20000.00 0.0008
328.15 25000.00 0.0008
328.15 30000.00 0.0008
328.15 35000.00 0.0008
328.15 40000.00 0.0007
328.15 45000.00 0.0007
328.15 50000.00 0.0007
328.15 55000.00 0.0007
338.15 5000.00 0.0009
338.15 10000.00 0.0009
338.15 15000.00 0.0008
338.15 20000.00 0.0008
338.15 25000.00 0.0008
338.15 30000.00 0.0008
338.15 35000.00 0.0008
338.15 40000.00 0.0007
338.15 45000.00 0.0007
338.15 50000.00 0.0007
338.15 55000.00 0.0007
348.15 5000.00 0.0009
348.15 10000.00 0.0009
348.15 15000.00 0.0009
348.15 20000.00 0.0008
348.15 25000.00 0.0008
348.15 30000.00 0.0008
348.15 35000.00 0.0008
348.15 40000.00 0.0008
348.15 45000.00 0.0007
348.15 50000.00 0.0007
348.15 55000.00 0.0007
Reference

Mass density, kg/m3

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
298.15 100.00 821.4
Reference
Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
278.15 100.00 835.2
278.15 1000.00 835.7
278.15 5000.00 838.0
278.15 10000.00 841.0
278.15 15000.00 843.7
278.15 20000.00 846.4
278.15 25000.00 849.0
278.15 30000.00 851.5
278.15 35000.00 854.0
278.15 40000.00 856.4
278.15 45000.00 858.8
278.15 50000.00 861.1
278.15 55000.00 863.4
278.15 60000.00 865.5
288.15 100.00 828.4
288.15 1000.00 829.0
288.15 5000.00 831.5
288.15 10000.00 834.4
288.15 15000.00 837.3
288.15 20000.00 840.1
288.15 25000.00 842.8
288.15 30000.00 845.5
288.15 35000.00 848.0
288.15 40000.00 850.5
288.15 45000.00 852.9
288.15 50000.00 855.3
288.15 55000.00 857.6
288.15 60000.00 859.8
298.15 100.00 821.4
298.15 1000.00 822.0
298.15 5000.00 824.6
298.15 10000.00 827.7
298.15 15000.00 830.7
298.15 20000.00 833.6
298.15 25000.00 836.4
298.15 30000.00 839.1
298.15 35000.00 841.8
298.15 40000.00 844.4
298.15 45000.00 846.9
298.15 50000.00 849.4
298.15 55000.00 851.7
298.15 60000.00 853.9
308.15 100.00 814.5
308.15 1000.00 815.1
308.15 5000.00 817.8
308.15 10000.00 821.1
308.15 15000.00 824.2
308.15 20000.00 827.2
308.15 25000.00 830.1
308.15 30000.00 833.0
308.15 35000.00 835.7
308.15 40000.00 838.4
308.15 45000.00 841.0
308.15 50000.00 843.5
308.15 55000.00 846.0
308.15 60000.00 848.2
318.15 100.00 807.5
318.15 1000.00 808.1
318.15 5000.00 811.0
318.15 10000.00 814.4
318.15 15000.00 817.7
318.15 20000.00 820.8
318.15 25000.00 823.8
318.15 30000.00 826.8
318.15 35000.00 829.6
318.15 40000.00 832.4
318.15 45000.00 835.1
318.15 50000.00 837.7
318.15 55000.00 840.3
318.15 60000.00 842.6
328.15 100.00 800.4
328.15 1000.00 801.1
328.15 5000.00 804.1
328.15 10000.00 807.7
328.15 15000.00 811.1
328.15 20000.00 814.4
328.15 25000.00 817.5
328.15 30000.00 820.5
328.15 35000.00 823.5
328.15 40000.00 826.4
328.15 45000.00 829.1
328.15 50000.00 831.9
328.15 55000.00 834.5
328.15 60000.00 836.9
338.15 100.00 793.2
338.15 1000.00 793.9
338.15 5000.00 796.9
338.15 10000.00 800.8
338.15 15000.00 804.4
338.15 20000.00 807.8
338.15 25000.00 811.1
338.15 30000.00 814.2
338.15 35000.00 817.3
338.15 40000.00 820.3
338.15 45000.00 823.1
338.15 50000.00 825.9
338.15 55000.00 828.7
338.15 60000.00 831.2
348.15 100.00 785.6
348.15 1000.00 786.4
348.15 5000.00 789.8
348.15 10000.00 793.6
348.15 15000.00 797.4
348.15 20000.00 801.0
348.15 25000.00 804.5
348.15 30000.00 807.8
348.15 35000.00 810.9
348.15 40000.00 814.0
348.15 45000.00 817.0
348.15 50000.00 819.9
348.15 55000.00 822.7
348.15 60000.00 825.5
358.15 100.00 778.0
358.15 1000.00 778.8
358.15 5000.00 782.3
358.15 10000.00 786.4
358.15 15000.00 790.4
358.15 20000.00 794.1
358.15 25000.00 797.7
358.15 30000.00 801.1
358.15 35000.00 804.5
358.15 40000.00 807.7
358.15 45000.00 810.8
358.15 50000.00 813.6
358.15 55000.00 816.7
358.15 60000.00 819.6
Reference
Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
298.15 2000.00 823.6
298.15 4010.00 824.8
298.15 6000.00 826.0
298.15 8000.00 827.2
298.15 10000.00 828.4
298.15 13010.00 830.1
298.15 16010.00 831.8
298.15 18990.00 833.4
298.15 22010.00 835.0
298.15 25010.00 836.6
298.15 28010.00 838.3
298.15 30010.00 839.3
303.15 1990.00 819.4
303.15 3990.00 820.6
303.15 5980.00 821.9
303.16 7980.00 823.1
303.15 10010.00 824.4
303.16 13000.00 826.2
303.15 16020.00 827.9
303.15 19030.00 829.7
303.16 22010.00 831.3
303.15 25000.00 833.0
303.16 28000.00 834.6
303.15 29980.00 835.6
313.15 1970.00 812.3
313.15 4000.00 813.6
313.15 6010.00 815.0
313.15 8000.00 816.3
313.15 10010.00 817.5
313.15 13030.00 819.4
313.15 15980.00 821.2
313.15 18990.00 823.0
313.15 21990.00 824.8
313.15 25000.00 826.5
313.15 27980.00 828.2
313.15 29990.00 829.3
323.15 2010.00 805.6
323.15 4010.00 807.0
323.15 6010.00 808.4
323.15 8000.00 809.7
323.15 10010.00 811.1
323.15 13020.00 813.0
323.15 16020.00 814.9
323.15 19010.00 816.8
323.15 22000.00 818.6
323.15 25010.00 820.4
323.15 28010.00 822.1
323.15 30020.00 823.3
Reference
Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
298.15 100.00 821.4
Reference
Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
313.14 1004.00 811.26
313.14 2019.00 811.95
313.14 3000.00 812.59
313.14 4020.00 813.22
313.14 4995.00 813.89
313.14 6000.00 814.53
313.14 7007.00 815.21
313.14 8012.00 815.83
313.14 8994.00 816.51
313.14 10014.00 817.19
313.14 11007.00 817.79
313.14 12000.00 818.42
313.14 12997.00 819.05
313.14 14001.00 819.67
313.14 14997.00 820.27
313.14 16002.00 820.89
313.14 17001.00 821.48
313.14 17997.00 822.1
313.14 19004.00 822.69
313.14 20007.00 823.28
313.14 21004.00 823.86
323.09 1007.00 804.26
323.09 2016.00 804.97
323.09 3019.00 805.7
323.09 4025.00 806.4
323.09 5012.00 807.07
323.09 6093.00 807.82
323.09 7143.00 808.56
323.09 8009.00 809.12
323.09 8989.00 809.77
323.09 10014.00 810.47
323.09 11031.00 811.14
323.09 12010.00 811.82
323.09 13005.00 812.44
323.09 14003.00 813.11
323.09 15012.00 813.76
323.09 16009.00 814.4
323.09 17005.00 815.04
323.09 18013.00 815.66
323.09 19003.00 816.26
323.09 20025.00 816.9
323.09 21081.00 817.56
323.09 22009.00 818.09
333.05 1038.00 797.31
333.05 2029.00 798.03
333.05 2999.00 798.76
333.05 4033.00 799.51
333.05 5020.00 800.25
333.05 6014.00 800.97
333.05 7029.00 801.69
333.05 8011.00 802.44
333.05 9005.00 803.11
333.05 10022.00 803.83
333.05 11011.00 804.55
333.05 12021.00 805.23
333.05 13022.00 805.92
333.05 14031.00 806.61
333.05 15010.00 807.28
333.05 16023.00 807.92
333.05 17012.00 808.59
333.05 18035.00 809.23
333.05 19009.00 809.87
333.05 20002.00 810.51
333.05 21011.00 811.15
333.05 22019.00 811.82
343.03 1049.00 790.6
343.03 2003.00 791.16
343.03 2981.00 791.93
343.03 4017.00 792.68
343.03 5000.00 793.37
343.03 6005.00 794.05
343.03 7018.00 794.88
343.03 8104.00 795.68
343.03 9014.00 796.44
343.03 10022.00 797.1
343.03 11028.00 797.87
343.03 11997.00 798.58
343.03 13030.00 799.3
343.03 14005.00 800.0
343.03 15002.00 800.66
343.03 16032.00 801.38
343.03 17016.00 801.99
343.03 18012.00 802.68
343.03 19005.00 803.29
343.03 20018.00 803.98
343.03 21014.00 804.61
343.03 22004.00 805.23
352.89 1023.00 782.71
352.89 2011.00 783.55
352.89 3032.00 784.42
352.89 4022.00 785.42
352.89 5005.00 786.18
352.89 6026.00 787.13
352.89 7003.00 787.9
352.89 8016.00 788.71
352.89 9007.00 789.47
352.89 10003.00 790.22
352.89 11022.00 791.0
352.89 12170.00 791.78
352.89 13015.00 792.51
352.89 14018.00 793.24
352.89 15009.00 794.0
352.89 16023.00 794.74
352.89 17010.00 795.48
352.89 18002.00 796.16
352.89 19029.00 796.9
352.89 20046.00 797.63
352.89 21023.00 798.3
362.77 1051.00 775.67
362.77 2025.00 776.41
362.77 3016.00 777.19
362.77 4009.00 778.05
362.77 4974.00 778.77
362.77 6005.00 779.51
362.77 7006.00 780.3
362.77 8011.00 780.95
362.77 9008.00 781.79
362.77 10034.00 782.62
362.77 11013.00 783.32
362.77 11987.00 784.03
362.77 13015.00 784.77
362.77 14006.00 785.51
362.77 14997.00 786.3
362.77 16001.00 787.03
362.77 17013.00 787.79
362.77 17997.00 788.55
362.77 19000.00 789.33
362.77 20023.00 790.04
362.77 21004.00 790.83
Reference

Thermal conductivity, W/m/K

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Thermal conductivity, W/m/K - Liquid
274.92 100.00 0.1580
274.85 5000.00 0.1598
274.82 10000.00 0.1611
274.77 20000.00 0.1639
274.63 30000.00 0.1669
294.93 100.00 0.1545
294.62 5000.00 0.1560
294.61 10100.00 0.1576
294.59 20100.00 0.1606
294.58 30000.00 0.1634
314.41 100.00 0.1511
314.95 5000.00 0.1530
314.91 10000.00 0.1545
314.86 20000.00 0.1578
314.86 30000.00 0.1609
334.98 100.00 0.1471
334.92 5000.00 0.1490
334.90 10000.00 0.1509
334.84 20000.00 0.1544
334.83 30000.00 0.1576
354.98 100.00 0.1427
354.41 5000.00 0.1445
354.36 10000.00 0.1466
354.50 20000.00 0.1505
354.35 30000.00 0.1539
374.96 100.00 0.1380
374.43 5100.00 0.1400
374.41 10000.00 0.1421
374.81 20000.00 0.1464
374.84 30000.00 0.1503
394.88 300.00 0.1325
395.13 5000.00 0.1349
395.05 10000.00 0.1377
394.82 20000.00 0.1420
394.85 30000.00 0.1461
Reference

Correlations

Property Value Unit Temperature (K) Source
Pvap [1.33; 202.64] kPa [358.71; 495.05] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Pvp) = A + B/(T + C)
Coefficient A1.45038e+01
Coefficient B-3.54647e+03
Coefficient C-1.09245e+02
Temperature range, min.358.71
Temperature range, max.495.05
Pvap 1.33 kPa 358.71 Calculated Property
Pvap 3.01 kPa 373.86 Calculated Property
Pvap 6.22 kPa 389.01 Calculated Property
Pvap 11.92 kPa 404.16 Calculated Property
Pvap 21.45 kPa 419.31 Calculated Property
Pvap 36.55 kPa 434.45 Calculated Property
Pvap 59.38 kPa 449.60 Calculated Property
Pvap 92.58 kPa 464.75 Calculated Property
Pvap 139.18 kPa 479.90 Calculated Property
Pvap 202.64 kPa 495.05 Calculated Property
Pvap [7.80e-05; 2692.59] kPa [257.65; 652.50] KDB Vapor Pressure Data Show Hide
Equationln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A2.04801e+02
Coefficient B-1.63274e+04
Coefficient C-2.73260e+01
Coefficient D1.22481e-05
Temperature range, min.257.65
Temperature range, max.652.50
Pvap 7.80e-05 kPa 257.65 Calculated Property
Pvap 0.01 kPa 301.52 Calculated Property
Pvap 0.49 kPa 345.39 Calculated Property
Pvap 5.66 kPa 389.27 Calculated Property
Pvap 33.30 kPa 433.14 Calculated Property
Pvap 124.61 kPa 477.01 Calculated Property
Pvap 343.81 kPa 520.88 Calculated Property
Pvap 771.79 kPa 564.76 Calculated Property
Pvap 1508.48 kPa 608.63 Calculated Property
Pvap 2692.59 kPa 652.50 Calculated Property

Similar Compounds

1-Tetracosanol. 1-Tricosanol. Heptadecanol. 1-Eicosanol. 1-Tetradecanol. n-Heptadecanol-1. 1-Dodecanol. 1-Octadecanol. 1-Undecanol. Behenic alcohol. n-Nonadecanol-1. 1-Decanol. 1-PENTACOSANOL. 1-Heptacosanol. 1-Heneicosanol.

Find more compounds similar to 1-Octanol.

Mixtures

Find more mixtures with 1-Octanol.

Sources

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