Chemical Properties of 1-Decanol (CAS 112-30-1)

1-Decanol

InChI
InChI=1S/C10H22O/c1-2-3-4-5-6-7-8-9-10-11/h11H,2-10H2,1H3
InChI Key
MWKFXSUHUHTGQN-UHFFFAOYSA-N
Formula
C10H22O
SMILES
CCCCCCCCCCO
Molecular Weight1
158.28
CAS
112-30-1
Other Names
  • 1-Hydroxydecane
  • Agent 504
  • Alcohol C10
  • Alfol 10
  • Antak
  • C 10 alcohol
  • Capric alcohol
  • Caprinic alcohol
  • Conol 10N
  • Decanol
  • Decanol-(1)
  • Decyl, n- alcohol
  • Decylic Alcohol
  • Dytol S-91
  • Epal 10
  • Kalcohl 10H
  • Lorol 22
  • Lorol C10
  • NSC 406313
  • Nacol 10-99
  • Nonylcacarbinol
  • Nonylcarbinol
  • Primary decyl alcohol
  • Royaltac
  • Royaltac M-2
  • Royaltac-85
  • Sipol L10
  • T-148
  • decan-1-ol
  • decyl alcohol
  • n-Decan-1-ol
  • n-Decanol
  • n-decyl 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 0.6070 ChemSep v8.3 pure component data
ΔcH°liquid [-6619.00; -6593.10] kJ/mol Show Hide
ΔcH°liquid -6619.00 ± 8.00 kJ/mol NIST
ΔcH°liquid -6601.10 ± 1.10 kJ/mol NIST
ΔcH°liquid -6599.63 ± 0.75 kJ/mol NIST
ΔcH°liquid -6593.30 ± 3.30 kJ/mol NIST
ΔcH°liquid -6593.10 kJ/mol NIST
μ [1.62; 1.80] debye Show Hide
μ 1.62 debye ChemSep v8.3 pure component data
μ 1.80 debye KDB
η 0.0111922 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
Tflash,cc 355.37 K KDB
ΔfG° [-104.30; -100.20] kJ/mol Show Hide
ΔfG° -100.20 kJ/mol ChemSep v8.3 pure component data
ΔfG° -104.30 kJ/mol KDB
ΔfH°gas [-404.60; -387.20] kJ/mol Show Hide
ΔfH°gas -398.50 kJ/mol ChemSep v8.3 pure component data
ΔfH°gas -401.90 kJ/mol KDB
ΔfH°gas -387.20 kJ/mol NIST
ΔfH°gas -396.60 ± 1.40 kJ/mol NIST
ΔfH°gas -388.80 kJ/mol NIST
ΔfH°gas -398.20 ± 1.20 kJ/mol NIST
ΔfH°gas -395.20 ± 2.40 kJ/mol NIST
ΔfH°gas -404.60 ± 3.10 kJ/mol NIST
ΔfH°liquid [-486.10; -478.10] kJ/mol Show Hide
ΔfH°liquid -478.10 ± 1.10 kJ/mol NIST
ΔfH°liquid -479.74 ± 0.96 kJ/mol NIST
ΔfH°liquid -486.10 ± 3.30 kJ/mol NIST
ΔfH°liquid -486.10 ± 3.00 kJ/mol NIST
ΔfusH° [31.40; 33.67] kJ/mol Show Hide
ΔfusH° 33.67 kJ/mol Heat Capacities and Derived Thermodynamic Functions of 1-Hexanol, 1-Heptanol, 1-Octanol, and 1-Decanol between 5 K and 390 K
ΔfusH° 31.40 kJ/mol Measurements, Correlations, and Mod. UNIFAC (Do) Prediction of (Solid-Liquid) Phase Equilibria Diagrams in Binary Systems (Aliphatic Ketone + an Alcohol)
ΔsubH° 112.50 ± 6.30 kJ/mol NIST
ΔvapH° [77.80; 90.90] kJ/mol Show Hide
ΔvapH° 81.50 kJ/mol NIST
ΔvapH° 80.90 kJ/mol NIST
ΔvapH° 81.70 kJ/mol NIST
ΔvapH° 79.30 kJ/mol NIST
ΔvapH° 81.49 ± 0.78 kJ/mol NIST
ΔvapH° 81.50 ± 0.80 kJ/mol NIST
ΔvapH° 81.50 ± 0.75 kJ/mol NIST
ΔvapH° 81.50 ± 0.80 kJ/mol NIST
ΔvapH° 77.80 ± 0.80 kJ/mol NIST
ΔvapH° 82.90 ± 2.10 kJ/mol NIST
ΔvapH° Outlier 90.90 kJ/mol NIST
IE 9.92 eV Relay (1.0) Calculated Property
log10WS [-3.63; -3.63]   Show Hide
log10WS -3.63 Aq. Solubility Prediction
log10WS -3.63 Estimated Solubility
logPoct/wat 3.119 Crippen Calculated Property
McVol 157.630 ml/mol McGowan Calculated Property
NFPA Fire 2 KDB
Pc [2308.00; 2320.00] kPa Show Hide
Pc 2308.00 kPa ChemSep v8.3 pure component data
Pc 2315.00 kPa KDB
Pc 2320.00 ± 50.00 kPa NIST
Pc 2310.00 ± 60.00 kPa NIST
Pc 2320.00 ± 20.00 kPa NIST
Pc 2320.00 ± 20.00 kPa NIST
Ptriple [1.00e-04; 1.51e-04] kPa Show Hide
Ptriple 1.51e-04 kPa ChemSep v8.3 pure component data
Ptriple 1.00e-04 ± 1.30e-05 kPa NIST
ρc [243.75; 264.33] kg/m3 Show Hide
ρc 243.75 ± 7.91 kg/m3 NIST
ρc 264.33 kg/m3 NIST
ρc 243.75 ± 6.33 kg/m3 NIST
ρc 264.33 ± 3.17 kg/m3 NIST
Inp [215.20; 1287.00]   Show Hide
Inp 1271.19 NIST
Inp 1255.70 NIST
Inp 1280.00 NIST
Inp 1262.00 NIST
Inp 1254.00 NIST
Inp 1254.00 NIST
Inp 1254.00 NIST
Inp 1255.00 NIST
Inp 1255.00 NIST
Inp 1255.00 NIST
Inp 1255.00 NIST
Inp 1256.00 NIST
Inp 1262.00 NIST
Inp 1262.00 NIST
Inp 1262.00 NIST
Inp 1249.00 NIST
Inp 1247.00 NIST
Inp 1247.00 NIST
Inp 1244.00 NIST
Inp 1247.00 NIST
Inp 1241.00 NIST
Inp 1256.00 NIST
Inp 1246.00 NIST
Inp 1252.00 NIST
Inp 1260.00 NIST
Inp 1253.00 NIST
Inp 1264.00 NIST
Inp 1262.00 NIST
Inp 1264.00 NIST
Inp 1276.00 NIST
Inp 1263.00 NIST
Inp 1259.00 NIST
Inp 1255.00 NIST
Inp 1257.00 NIST
Inp 1257.00 NIST
Inp 1272.00 NIST
Inp 1256.00 NIST
Inp 1272.00 NIST
Inp 1275.00 NIST
Inp 1275.00 NIST
Inp 1279.00 NIST
Inp 1272.00 NIST
Inp 1255.20 NIST
Inp 1273.80 NIST
Inp 1258.00 NIST
Inp 1281.00 NIST
Inp 1272.00 NIST
Inp 1272.00 NIST
Inp 1285.00 NIST
Inp 1259.00 NIST
Inp 1273.00 NIST
Inp 1274.00 NIST
Inp 1267.00 NIST
Inp 1256.90 NIST
Inp 1258.90 NIST
Inp 1269.00 NIST
Inp 1274.00 NIST
Inp 1282.50 NIST
Inp 1264.00 NIST
Inp 1254.00 NIST
Inp 1259.00 NIST
Inp 1271.00 NIST
Inp 1269.00 NIST
Inp 1267.00 NIST
Inp 1267.00 NIST
Inp 1273.00 NIST
Inp 1274.00 NIST
Inp 1275.00 NIST
Inp 1271.00 NIST
Inp 1273.00 NIST
Inp 1273.00 NIST
Inp 1273.00 NIST
Inp 1274.00 NIST
Inp 1274.00 NIST
Inp 1274.00 NIST
Inp 1274.00 NIST
Inp 1274.00 NIST
Inp 1275.00 NIST
Inp 1276.00 NIST
Inp 1278.00 NIST
Inp 1274.00 NIST
Inp 1263.00 NIST
Inp 1278.00 NIST
Inp 1272.00 NIST
Inp 1272.00 NIST
Inp 1255.00 NIST
Inp 1255.00 NIST
Inp 1270.00 NIST
Inp 1270.00 NIST
Inp 1275.00 NIST
Inp 1275.00 NIST
Inp 1272.00 NIST
Inp 1270.00 NIST
Inp 1272.00 NIST
Inp 1263.00 NIST
Inp 1266.00 NIST
Inp 1272.00 NIST
Inp 1266.00 NIST
Inp 1269.00 NIST
Inp 1254.00 NIST
Inp 1263.00 NIST
Inp 1257.00 NIST
Inp 1255.00 NIST
Inp 1266.00 NIST
Inp 1275.00 NIST
Inp 1279.00 NIST
Inp 1283.00 NIST
Inp 1259.00 NIST
Inp 1279.00 NIST
Inp 1281.00 NIST
Inp 1285.00 NIST
Inp 1261.00 NIST
Inp 1269.00 NIST
Inp 1263.00 NIST
Inp 1272.00 NIST
Inp 1272.00 NIST
Inp 1287.00 NIST
Inp 1270.00 NIST
Inp 1281.00 NIST
Inp 1284.00 NIST
Inp 1287.00 NIST
Inp 1261.00 NIST
Inp 1269.00 NIST
Inp 1272.00 NIST
Inp 1264.00 NIST
Inp 1263.00 NIST
Inp 1256.00 NIST
Inp 1272.10 NIST
Inp 1259.00 NIST
Inp 1259.00 NIST
Inp 1257.00 NIST
Inp 1257.00 NIST
Inp 1263.00 NIST
Inp 1283.00 NIST
Inp 1257.00 NIST
Inp 1249.00 NIST
Inp 1261.00 NIST
Inp Outlier 215.20 NIST
Inp Outlier 216.62 NIST
Inp Outlier 216.09 NIST
Inp 1274.00 NIST
Inp 1271.00 NIST
Inp Outlier 215.20 NIST
Inp 1272.00 NIST
Inp 1279.00 NIST
Inp 1281.00 NIST
Inp 1273.00 NIST
Inp 1269.00 NIST
Inp 1271.19 NIST
Inp 1254.00 NIST
Inp 1255.00 NIST
Inp 1249.00 NIST
Inp 1241.00 NIST
Inp 1253.00 NIST
Inp 1263.00 NIST
Inp 1266.00 NIST
Inp 1259.00 NIST
Inp 1283.00 NIST
I [1714.00; 1783.00]   Show Hide
I 1756.00 NIST
I 1760.00 NIST
I 1783.00 NIST
I 1724.00 NIST
I 1769.00 NIST
I 1746.00 NIST
I 1726.00 NIST
I 1760.00 NIST
I 1759.00 NIST
I 1753.00 NIST
I 1764.00 NIST
I 1783.00 NIST
I 1750.00 NIST
I 1740.00 NIST
I 1732.00 NIST
I 1736.00 NIST
I 1740.00 NIST
I 1757.00 NIST
I 1757.00 NIST
I 1769.00 NIST
I 1759.00 NIST
I 1763.00 NIST
I 1767.00 NIST
I 1760.00 NIST
I 1771.00 NIST
I Outlier 1714.00 NIST
I 1763.00 NIST
I 1748.00 NIST
I 1744.00 NIST
I 1745.00 NIST
I 1748.00 NIST
I 1748.00 NIST
I 1735.00 NIST
I 1735.00 NIST
I 1763.00 NIST
I 1764.90 NIST
I 1770.00 NIST
I 1765.00 NIST
I 1770.00 NIST
I 1752.00 NIST
I 1751.00 NIST
I 1726.00 NIST
I 1756.00 NIST
I 1729.00 NIST
I 1767.00 NIST
I 1761.00 NIST
I 1764.00 NIST
I 1760.00 NIST
I 1767.00 NIST
I 1778.00 NIST
I 1768.00 NIST
I 1769.00 NIST
I 1783.00 NIST
I Outlier 1723.00 NIST
I 1766.00 NIST
I 1766.00 NIST
I 1753.00 NIST
I 1778.00 NIST
I 1781.00 NIST
I 1752.00 NIST
I 1752.00 NIST
I 1781.00 NIST
I 1781.00 NIST
I 1765.00 NIST
I 1781.00 NIST
I 1750.00 NIST
I 1766.00 NIST
I 1766.00 NIST
I 1735.00 NIST
I 1752.00 NIST
I 1757.00 NIST
I 1767.00 NIST
I 1748.00 NIST
I 1735.00 NIST
I 1765.00 NIST
I 1724.00 NIST
I 1759.00 NIST
I 1740.00 NIST
Tboil [476.00; 506.10] K Show Hide
Tboil 503.70 K Phase equilibria of (water + levunilic acid + alcohol) ternary systems
Tboil 503.70 K (Liquid + liquid) equilibria of (water + propionic acid + alcohol) ternary systems
Tboil 503.70 K (Liquid + liquid) equilibria of (water + lactic acid + alcohol) ternary systems
Tboil 502.95 K Study of a Binary Liquid Mixture of Diethylamine and 1-Decanol and Validation of Theoretical Approaches of Sound Speed at Different Temperatures
Tboil 503.00 K ChemSep v8.3 pure component data
Tboil 504.20 K KDB
Tboil 504.20 K NIST
Tboil 504.15 ± 0.50 K NIST
Tboil 504.45 ± 2.00 K NIST
Tboil 502.99 ± 2.00 K NIST
Tboil 505.95 ± 2.00 K NIST
Tboil 502.15 ± 3.00 K NIST
Tboil 503.65 ± 3.00 K NIST
Tboil 502.65 ± 4.00 K NIST
Tboil 504.65 ± 4.00 K NIST
Tboil 503.15 ± 4.00 K NIST
Tboil 505.95 ± 0.40 K NIST
Tboil 506.10 ± 0.50 K NIST
Tboil 506.05 ± 1.00 K NIST
Tboil 506.10 ± 0.50 K NIST
Tboil 506.10 ± 0.50 K NIST
Tboil 504.15 ± 3.00 K NIST
Tboil Outlier 476.00 ± 5.00 K NIST
Tc [687.00; 708.00] K Show Hide
Tc 688.00 K ChemSep v8.3 pure component data
Tc 687.30 K KDB
Tc 687.00 ± 1.00 K NIST
Tc 687.70 ± 1.00 K NIST
Tc 687.00 ± 0.70 K NIST
Tc 687.00 ± 0.60 K NIST
Tc 687.10 K NIST
Tc 687.30 ± 1.30 K NIST
Tc 687.00 K NIST
Tc Outlier 708.00 ± 2.00 K NIST
Tfus [276.15; 280.51] K Show Hide
Tfus 280.15 K Experimental solid-liquid phase equilibria of {cholesterol + binary solvent mixture: 1-Alcohol (C4-C10) + cyclohexane}
Tfus 280.19 K SLE and LLE for tri-butylphosphate or tri-octylamine contained systems; extractive solvents of Molybdenum
Tfus 280.10 K (Solid + liquid) equilibrium phase diagrams in binary mixtures containing terpenes: New experimental data and analysis of several modelling strategies with modified UNIFAC (Dortmund) and PC-SAFT equation of state
Tfus 278.20 K Phase equilibria of didecyldimethylammonium nitrate ionic liquid with water and organic solvents
Tfus Outlier 276.15 K The manufacture of organic carbonate-poly(methyl ethylacrylate) nanowebs with thermal buffering effect
Tfus 278.67 K Experimental (Solid + Liquid) and (Liquid + Liquid) Equilibria and Excess Molar Volume of Alkanol + Acetonitrile, Propanenitrile, and Butanenitrile Mixtures
Tfus 280.51 K Phase Equilibria Study of the Binary Systems (N-Butyl-4-methylpyridinium Tosylate Ionic Liquid + Organic Solvent, or Water)
Tfus 280.19 K Solid-Liquid Equilibria, Excess Molar Volumes, and Molar Refractivity Deviations for Extractive Solvents of Molybdenum
Tfus 280.05 K ChemSep v8.3 pure component data
Tfus 280.00 K KDB
Tfus 279.87 K Aq. Solubility Prediction
Tfus 279.60 ± 0.50 K NIST
Tfus 280.05 ± 0.40 K NIST
Tfus 277.00 ± 3.00 K NIST
Ttriple [275.64; 280.05] K Show Hide
Ttriple 275.64 K Solid-liquid phase equilibrium diagrams of binary mixtures containing fatty acids, fatty alcohol compounds and tripalmitin using differential scanning calorimetry
Ttriple 280.05 K ChemSep v8.3 pure component data
Ttriple 279.65 ± 1.00 K NIST
UQi 6.91 ChemSep v8.3 pure component data
URi 7.97 ChemSep v8.3 pure component data
Vc [0.645; 0.649] m3/kmol Show Hide
Vc 0.645 m3/kmol ChemSep v8.3 pure component data
Vc 0.649 m3/kmol KDB
Vc 0.649 m3/kmol NIST
Zc [0.2600000; 0.2629130]   Show Hide
Zc 0.2600000 ChemSep v8.3 pure component data
Zc 0.2629130 KDB

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,liquid [369.96; 387.80] J/mol×K [298.15; 305.79] Show Hide
Cp,liquid 372.98 J/mol×K 298.15 NIST
Cp,liquid 369.96 J/mol×K 298.15 NIST
Cp,liquid 377.00 J/mol×K 301.00 NIST
Cp,liquid 377.30 J/mol×K 303.15 NIST
Cp,liquid 387.80 J/mol×K 304.05 NIST
Cp,liquid 377.80 J/mol×K 305.79 NIST
η [0.0023990; 0.0220640] Pa×s [283.15; 348.15] Show Hide
η 0.0220640 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 0.0220640 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 0.0179880 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 0.0144990 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 0.0143870 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 0.0114710 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 0.0110900 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 0.0117350 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 0.0118250 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 0.0103000 Pa×s 300.00 Temperature and composition dependence of the density and viscosity of binary mixtures of (1-decanol + fragrance material)
η 0.0097150 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 0.0096100 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 0.0097160 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 0.0097540 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 0.0095610 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 0.0076320 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 0.0080000 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 0.0081350 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 0.0070900 Pa×s 310.00 Temperature and composition dependence of the density and viscosity of binary mixtures of (1-decanol + fragrance material)
η 0.0069000 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 0.0068420 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 0.0068200 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 0.0068190 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 0.0068310 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 0.0053750 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 0.0050000 Pa×s 320.00 Temperature and composition dependence of the density and viscosity of binary mixtures of (1-decanol + fragrance material)
η 0.0039280 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 0.0036700 Pa×s 330.00 Temperature and composition dependence of the density and viscosity of binary mixtures of (1-decanol + fragrance material)
η 0.0029640 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 0.0027400 Pa×s 340.00 Temperature and composition dependence of the density and viscosity of binary mixtures of (1-decanol + fragrance material)
η 0.0023990 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 7.74 298.15 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 [33.67; 37.66] kJ/mol [280.00; 280.10] Show Hide
ΔfusH 33.67 kJ/mol 280.00 NIST
ΔfusH 37.66 kJ/mol 280.10 NIST
ΔfusH 37.66 kJ/mol 280.10 NIST
ΔsubH 115.50 ± 6.30 kJ/mol 268.50 NIST
ΔvapH [50.21; 81.10] kJ/mol [304.00; 504.10] Show Hide
ΔvapH 79.50 kJ/mol 304.00 NIST
ΔvapH 77.60 kJ/mol 311.50 NIST
ΔvapH 77.60 kJ/mol 311.50 NIST
ΔvapH 78.20 ± 0.80 kJ/mol 323.00 NIST
ΔvapH 78.18 kJ/mol 323.15 NIST
ΔvapH 81.10 kJ/mol 328.00 NIST
ΔvapH 75.40 kJ/mol 335.50 NIST
ΔvapH 71.60 kJ/mol 379.50 NIST
ΔvapH 69.60 kJ/mol 412.50 NIST
ΔvapH 69.50 kJ/mol 441.00 NIST
ΔvapH 62.60 kJ/mol 466.50 NIST
ΔvapH 53.90 kJ/mol 501.50 NIST
ΔvapH 50.21 kJ/mol 504.10 KDB
Pvap [1.00e-03; 94.90] kPa [308.15; 501.05] Show Hide
Pvap 1.00e-03 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 4.00e-03 kPa 313.15 Isothermal (vapour + liquid) equilibrium at several temperatures of (1-chlorobutane + 1-octanol, or 1-decanol)
Pvap 4.00e-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 7.00e-03 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 7.00e-03 kPa 318.15 Isothermal (vapour + liquid) equilibrium at several temperatures of (1-chlorobutane + 1-octanol, or 1-decanol)
Pvap 0.01 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 0.01 kPa 323.15 Isothermal (vapour + liquid) equilibrium at several temperatures of (1-chlorobutane + 1-octanol, or 1-decanol)
Pvap 13.32 kPa 436.56 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
Pvap 40.00 kPa 469.23 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 39.99 kPa 469.52 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
Pvap 40.03 kPa 469.83 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 44.40 kPa 472.98 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 47.97 kPa 475.40 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 50.19 kPa 476.80 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 54.07 kPa 479.42 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 57.04 kPa 481.36 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 61.26 kPa 484.05 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 66.66 kPa 487.85 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
Pvap 67.43 kPa 487.90 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 73.44 kPa 491.16 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 76.32 kPa 492.56 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 79.92 kPa 494.46 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 85.24 kPa 496.88 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 94.90 kPa 501.05 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
n0 [1.43050; 1.43740]   [293.15; 308.15] Show Hide
n0 1.43706 293.15 Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrabromoethane and 1-alkanols binary mixtures
n0 1.43740 293.15 Distribution of Butyric Acid between Water and Several Solvents
n0 1.43700 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 1.43706 293.15 Excess molar volumes and viscosities of (1,1,2,2-tetrabromoethane + 1-alkanols) at T = (293.15 and 303.15) K
n0 1.43694 293.15 Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrachloroethane and 1-alkanols binary mixtures
n0 1.43520 298.15 Permittivities, Refractive Indices, Densities, and Excess Properties for Binary Systems Containing 1-Alkanols and Cyclopentanone
n0 1.43460 298.15 Densities, Viscosities, Speeds of Sound, and Refractive Indices of Binary Mixtures of 1-Decanol with Isomeric Chlorotoluenes
n0 1.43436 298.15 Liquid Liquid Phase Equilibria of 1-Propanol + Water + n-Alcohol Ternary Systems at 298.15 K and Atmospheric Pressure
n0 1.43456 298.15 Densities, Speeds of Sound, and Refractive Indices of Binary Mixtures of Decan-1-ol with Anisole, o-Cresol, m-Cresol, and p-Cresol at T = (298.15, 303.15, and 308.15) K
n0 1.43440 298.20 Ternary equilibrium data of mixtures consisting of 2-butanol, water, and heavy alcohols at T = 298.2 K
n0 1.43440 298.20 Tie-line data for water- formic acid-1-decanol ternary system at T = (298.2, 303.2, 313.2, 323.2) K
n0 1.43490 298.20 Solubility and Tie Line Data of the Water - Phosphoric Acid Solvents at T = (303.2 and 313.2) K: An Experimental and Correlational Study
n0 1.43256 303.15 Densities, Speeds of Sound, and Refractive Indices of Binary Mixtures of Decan-1-ol with Anisole, o-Cresol, m-Cresol, and p-Cresol at T = (298.15, 303.15, and 308.15) K
n0 1.43260 303.15 Densities, Viscosities, Speeds of Sound, and Refractive Indices of Binary Mixtures of 1-Decanol with Isomeric Chlorotoluenes
n0 1.43364 303.15 Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrachloroethane and 1-alkanols binary mixtures
n0 1.43266 303.15 Densities, Speeds of Sound, and Refractive Indices of Binary Mixtures of Decan-1-ol with Anisole, o-Cresol, m-Cresol, and p-Cresol at T = (298.15, 303.15, and 308.15) K
n0 1.43302 303.15 Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrabromoethane and 1-alkanols binary mixtures
n0 1.43050 308.15 Densities, Viscosities, Speeds of Sound, and Refractive Indices of Binary Mixtures of 1-Decanol with Isomeric Chlorotoluenes
n0 1.43050 308.15 Densities, Speeds of Sound, and Refractive Indices of Binary Mixtures of Decan-1-ol with Anisole, o-Cresol, m-Cresol, and p-Cresol at T = (298.15, 303.15, and 308.15) K
ρl [780.34; 836.51] kg/m3 [283.15; 363.15] Show Hide
ρl 836.51 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 833.14 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 830.00 kg/m3 293.00 KDB
ρl 829.50 kg/m3 293.15 Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl 829.76 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 829.99 kg/m3 293.15 Thermophysical and sonochemical behaviour of binary mixtures of decan-1-ol with halohydrocarbons at (T = 293.15 and 313.15) K
ρl 829.95 kg/m3 293.15 Thermodynamics of 1-alkanol + linear polyether mixtures
ρl 829.50 kg/m3 293.15 Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl 829.97 kg/m3 293.15 Thermodynamics of mixtures with strongly negative deviations from Raoult s law. XII. Densities, viscosities and refractive indices at T = (293.15 to 303.15) K for (1-heptanol, or 1-decanol + cyclohexylamine) systems. Application of the ERAS model to (1-alkanol + cyclohexylamine) mixtures
ρl 829.76 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 827.21 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 826.58 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 826.36 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 826.38 kg/m3 298.15 Phase behaviour of ionic liquid 1-butyl-1-methylpyrrolidinium tris(pentafluoroethyl)trifluorophosphate with alcohols, water and aromatic hydrocarbons
ρl 826.37 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 826.49 kg/m3 298.15 Thermodynamic, transport and excess properties of 2-butoxy ethanol +1-alkanol (C6,C8,C10) at different temperatures
ρl 826.41 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 826.10 kg/m3 298.15 Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl 826.58 kg/m3 298.15 Thermodynamics of mixtures with strongly negative deviations from Raoult s law. XII. Densities, viscosities and refractive indices at T = (293.15 to 303.15) K for (1-heptanol, or 1-decanol + cyclohexylamine) systems. Application of the ERAS model to (1-alkanol + cyclohexylamine) mixtures
ρl 826.31 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 826.38 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 826.38 kg/m3 298.15 Phase behaviour of tricyanomethanide-based ionic liquids with alcohols and hydrocarbons
ρl 826.42 kg/m3 298.15 Density and Relative Permittivity for 1-Alkanols + Dodecane at 298.15 K
ρl 826.64 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 826.90 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 826.47 kg/m3 298.15 Studies of thermophysical properties of binary liquid mixtures of amine and alcohols at various temperatures
ρl 826.56 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 826.95 kg/m3 298.15 Thermodynamics of 1-alkanol + linear polyether mixtures
ρl 826.74 kg/m3 298.15 Effect of chain length of alcohol on thermodynamic properties of their binary mixtures with benzylalcohol
ρl 826.10 kg/m3 298.15 Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl 826.41 kg/m3 298.20 Optimization and modeling of extraction equilibria of the type 2 ternary systems containing (water + isovaleric acid + solvent)
ρl 826.86 kg/m3 298.20 Experimental Data of Citric Acid Extraction from Aqueous Solution with 1-Decanol by Using Liquid-Liquid Equilibrium
ρl 822.89 kg/m3 303.15 Effect of chain length of alcohol on thermodynamic properties of their binary mixtures with benzylalcohol
ρl 822.95 kg/m3 303.15 Excess molar enthalpies and heat capacities of dimethyl sulfoxide + seven normal alkanols at 303.15K and atmospheric pressure
ρl 822.88 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 822.70 kg/m3 303.15 Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl 823.76 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 822.98 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 823.13 kg/m3 303.15 Thermodynamics of mixtures with strongly negative deviations from Raoult s law. XII. Densities, viscosities and refractive indices at T = (293.15 to 303.15) K for (1-heptanol, or 1-decanol + cyclohexylamine) systems. Application of the ERAS model to (1-alkanol + cyclohexylamine) mixtures
ρl 822.70 kg/m3 303.15 Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl 823.15 kg/m3 303.15 Thermodynamics of 1-alkanol + linear polyether mixtures
ρl 822.95 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 819.57 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 819.30 kg/m3 308.15 Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl 819.43 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 819.57 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 820.31 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 820.00 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 819.30 kg/m3 308.15 Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl 819.51 kg/m3 308.15 Effect of chain length of alcohol on thermodynamic properties of their binary mixtures with benzylalcohol
ρl 816.83 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 815.95 kg/m3 313.15 Effect of chain length of alcohol on thermodynamic properties of their binary mixtures with benzylalcohol
ρl 816.12 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 816.15 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 815.97 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 815.80 kg/m3 313.15 Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl 815.80 kg/m3 313.15 Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl 813.34 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 812.49 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 812.63 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 812.71 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 813.00 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 812.40 kg/m3 318.15 Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl 812.40 kg/m3 318.15 Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl 809.03 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 809.24 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 809.82 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 808.90 kg/m3 323.15 Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl 808.90 kg/m3 323.15 Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl 805.74 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 806.00 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 802.21 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 798.90 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 798.65 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 795.06 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 791.43 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 787.77 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 784.07 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 780.34 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 [1311.69; 1410.60] m/s [288.15; 318.18] Show Hide
csound,fluid 1410.60 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 1397.23 m/s 293.10 Excess molar heat capacities for (decan-1-ol + n-heptane) at temperatures from (290 to 318) K. Experimental results and theoretical description using the ERAS model
csound,fluid 1396.00 m/s 293.15 Densities, Speeds of Sound, and Isentropic Compressibilities of Binary Mixtures of {Alkan-1-ols + 1,2-Dimethylbenzene, or 1,3-Dimethylbenzene, or 1,4-Dimethylbenzene, or Ethylbenzene} at (293.15, 303.15, and 313.15) K
csound,fluid 1396.16 m/s 293.15 Thermodynamics of (1-alkanol + linear monoether) systems
csound,fluid 1396.65 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 1393.60 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 1379.96 m/s 298.07 Excess molar heat capacities for (decan-1-ol + n-heptane) at temperatures from (290 to 318) K. Experimental results and theoretical description using the ERAS model
csound,fluid 1380.58 m/s 298.15 Micellar Properties and Related Thermodynamic Parameters of Aqueous Anionic Surfactants in the Presence of Monohydric Alcohols
csound,fluid 1379.43 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 1378.90 m/s 298.15 Thermodynamics of (1-alkanol + linear monoether) systems
csound,fluid 1377.30 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 1362.82 m/s 303.04 Excess molar heat capacities for (decan-1-ol + n-heptane) at temperatures from (290 to 318) K. Experimental results and theoretical description using the ERAS model
csound,fluid 1359.80 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 1362.00 m/s 303.15 Densities, Speeds of Sound, and Isentropic Compressibilities of Binary Mixtures of {Alkan-1-ols + 1,2-Dimethylbenzene, or 1,3-Dimethylbenzene, or 1,4-Dimethylbenzene, or Ethylbenzene} at (293.15, 303.15, and 313.15) K
csound,fluid 1363.52 m/s 303.15 Micellar Properties and Related Thermodynamic Parameters of Aqueous Anionic Surfactants in the Presence of Monohydric Alcohols
csound,fluid 1362.40 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 1361.69 m/s 303.15 Thermodynamics of (1-alkanol + linear monoether) systems
csound,fluid 1345.82 m/s 308.04 Excess molar heat capacities for (decan-1-ol + n-heptane) at temperatures from (290 to 318) K. Experimental results and theoretical description using the ERAS model
csound,fluid 1345.62 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 1345.70 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 1346.58 m/s 308.15 Micellar Properties and Related Thermodynamic Parameters of Aqueous Anionic Surfactants in the Presence of Monohydric Alcohols
csound,fluid 1329.03 m/s 313.01 Excess molar heat capacities for (decan-1-ol + n-heptane) at temperatures from (290 to 318) K. Experimental results and theoretical description using the ERAS model
csound,fluid 1329.07 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 1329.00 m/s 313.15 Densities, Speeds of Sound, and Isentropic Compressibilities of Binary Mixtures of {Alkan-1-ols + 1,2-Dimethylbenzene, or 1,3-Dimethylbenzene, or 1,4-Dimethylbenzene, or Ethylbenzene} at (293.15, 303.15, and 313.15) K
csound,fluid 1326.70 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 1312.10 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
csound,fluid 1311.69 m/s 318.18 Excess molar heat capacities for (decan-1-ol + n-heptane) at temperatures from (290 to 318) K. Experimental results and theoretical description using the ERAS model
γ 0.03 N/m 293.20 KDB
ΔvapS 241.93 J/mol×K 323.15 NIST

Pressure Dependent Properties

Property Value Unit Pressure (kPa) Source
Tboilr 380.70 K 0.90 NIST

Datasets

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

Isobaric coefficient of expansion, 1/K

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Isobaric coefficient of expansion, 1/K - Liquid
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 0.0007
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 0.0008
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 0.0007
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 0.0007
328.15 35000.00 0.0007
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 0.0008
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 0.0007
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 0.0008
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 0.0007
348.15 45000.00 0.0007
348.15 50000.00 0.0007
348.15 55000.00 0.0007
Reference

Viscosity, Pa*s

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Viscosity, Pa*s - Liquid
298.15 2000.00 0.0113
298.15 3990.00 0.0115
298.15 6010.00 0.0118
298.15 8010.00 0.0121
298.15 10010.00 0.0123
298.15 13010.00 0.0127
298.15 16010.00 0.0132
298.15 19010.00 0.0136
298.15 22010.00 0.0140
298.15 25000.00 0.0145
298.15 28000.00 0.0149
298.15 29990.00 0.0152
303.15 1990.00 0.0089
303.15 4000.00 0.0091
303.15 5980.00 0.0093
303.15 8010.00 0.0096
303.15 10020.00 0.0098
303.15 12980.00 0.0101
303.15 15970.00 0.0104
303.15 19020.00 0.0108
303.15 22000.00 0.0111
303.15 24980.00 0.0114
303.15 27980.00 0.0118
303.15 30010.00 0.0120
313.15 2030.00 0.0062
313.15 4020.00 0.0064
313.15 6000.00 0.0065
313.15 7980.00 0.0067
313.15 9980.00 0.0068
313.15 12990.00 0.0071
313.15 15990.00 0.0073
313.15 18990.00 0.0075
313.15 22010.00 0.0078
313.15 25020.00 0.0080
313.15 28020.00 0.0082
313.15 29980.00 0.0084
323.15 2000.00 0.0047
323.15 4010.00 0.0049
323.15 6010.00 0.0050
323.15 8010.00 0.0051
323.15 9990.00 0.0052
323.15 13010.00 0.0054
323.15 16010.00 0.0055
323.15 19020.00 0.0057
323.15 22020.00 0.0059
323.15 25010.00 0.0061
323.15 28000.00 0.0062
323.15 30010.00 0.0064
Reference

Mass density, kg/m3

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
298.15 100.00 826.1
Reference
Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
288.15 100.00 832.3
288.15 1000.00 832.8
288.15 5000.00 835.2
288.15 10000.00 838.0
288.15 15000.00 840.8
288.15 20000.00 843.5
288.15 25000.00 846.1
288.15 30000.00 848.6
288.15 35000.00 851.1
288.15 40000.00 853.5
288.15 45000.00 855.9
288.15 50000.00 858.2
288.15 55000.00 860.4
288.15 60000.00 862.7
298.15 100.00 825.5
298.15 1000.00 826.0
298.15 5000.00 828.5
298.15 10000.00 831.5
298.15 15000.00 834.4
298.15 20000.00 837.2
298.15 25000.00 839.8
298.15 30000.00 842.5
298.15 35000.00 845.1
298.15 40000.00 847.6
298.15 45000.00 850.0
298.15 50000.00 852.4
298.15 55000.00 854.7
298.15 60000.00 856.8
308.15 100.00 818.7
308.15 1000.00 819.3
308.15 5000.00 821.9
308.15 10000.00 825.0
308.15 15000.00 828.0
308.15 20000.00 830.9
308.15 25000.00 833.7
308.15 30000.00 836.4
308.15 35000.00 839.1
308.15 40000.00 841.7
308.15 45000.00 844.2
308.15 50000.00 846.6
308.15 55000.00 849.0
308.15 60000.00 851.2
318.15 100.00 811.9
318.15 1000.00 812.5
318.15 5000.00 815.3
318.15 10000.00 818.5
318.15 15000.00 821.7
318.15 20000.00 824.7
318.15 25000.00 827.6
318.15 30000.00 830.4
318.15 35000.00 833.2
318.15 40000.00 835.8
318.15 45000.00 838.5
318.15 50000.00 841.0
318.15 55000.00 843.4
318.15 60000.00 845.7
328.15 100.00 805.0
328.15 1000.00 805.7
328.15 5000.00 808.5
328.15 10000.00 811.9
328.15 15000.00 815.2
328.15 20000.00 818.3
328.15 25000.00 821.4
328.15 30000.00 824.3
328.15 35000.00 827.1
328.15 40000.00 829.9
328.15 45000.00 832.6
328.15 50000.00 835.2
328.15 55000.00 837.7
328.15 60000.00 840.2
338.15 100.00 798.0
338.15 1000.00 798.7
338.15 5000.00 801.7
338.15 10000.00 805.2
338.15 15000.00 808.7
338.15 20000.00 812.0
338.15 25000.00 815.1
338.15 30000.00 818.1
338.15 35000.00 821.1
338.15 40000.00 824.0
338.15 45000.00 826.7
338.15 50000.00 829.4
338.15 55000.00 832.1
338.15 60000.00 834.5
348.15 100.00 790.9
348.15 1000.00 791.6
348.15 5000.00 794.8
348.15 10000.00 798.5
348.15 15000.00 802.0
348.15 20000.00 805.5
348.15 25000.00 808.8
348.15 30000.00 811.9
348.15 35000.00 815.0
348.15 40000.00 817.9
348.15 45000.00 820.8
348.15 50000.00 823.6
348.15 55000.00 826.4
348.15 60000.00 829.0
358.15 100.00 783.6
358.15 1000.00 784.3
358.15 5000.00 787.6
358.15 10000.00 791.6
358.15 15000.00 795.3
358.15 20000.00 798.9
358.15 25000.00 802.3
358.15 30000.00 805.6
358.15 35000.00 808.8
358.15 40000.00 811.9
358.15 45000.00 814.8
358.15 50000.00 817.7
358.15 55000.00 820.5
358.15 60000.00 822.9
Reference
Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
298.15 100.00 826.1
Reference
Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
313.12 1025.00 816.79
313.12 2002.00 817.46
313.12 2995.00 817.98
313.12 4013.00 818.58
313.12 5004.00 819.21
313.12 5994.00 819.86
313.12 7003.00 820.47
313.12 7997.00 821.19
313.12 9000.00 821.73
313.12 9994.00 822.38
313.12 10995.00 823.02
313.12 11995.00 823.67
313.12 12997.00 824.2
313.12 13996.00 824.82
313.12 14998.00 825.42
313.12 15990.00 826.01
313.12 16995.00 826.61
313.12 17986.00 827.14
313.12 18992.00 827.76
313.12 19993.00 828.31
313.12 20999.00 828.88
313.12 21509.00 829.19
323.09 1002.00 809.87
323.09 2011.00 810.59
323.09 3019.00 811.21
323.09 4014.00 811.83
323.09 5006.00 812.47
323.09 6012.00 813.18
323.09 7002.00 813.8
323.09 8003.00 814.42
323.09 9008.00 815.1
323.09 10006.00 815.7
323.09 11000.00 816.38
323.09 12002.00 816.97
323.09 13002.00 817.64
323.09 14000.00 818.21
323.09 15017.00 818.84
323.09 16003.00 819.4
323.09 17015.00 820.02
323.09 18006.00 820.61
323.09 19007.00 821.24
323.09 20007.00 821.84
323.09 21002.00 822.41
323.09 22014.00 823.01
333.04 1046.00 802.82
333.04 2018.00 803.5
333.04 3008.00 804.21
333.04 4012.00 804.88
333.04 5059.00 805.62
333.04 6016.00 806.29
333.04 7022.00 807.0
333.04 8014.00 807.64
333.04 9015.00 808.34
333.04 10015.00 808.97
333.04 11019.00 809.64
333.04 12007.00 810.31
333.04 13019.00 810.96
333.04 14019.00 811.6
333.04 15014.00 812.24
333.04 16021.00 812.88
333.04 17026.00 813.5
333.04 18023.00 814.11
333.04 19018.00 814.72
333.04 20025.00 815.35
333.04 21020.00 815.94
333.04 22032.00 816.58
342.98 1058.00 795.63
342.98 2045.00 796.4
342.98 3022.00 797.12
342.98 4035.00 797.9
342.98 5028.00 798.63
342.98 6030.00 799.37
342.98 7023.00 800.07
342.98 8028.00 800.78
342.98 9062.00 801.51
342.98 10035.00 802.22
342.98 11029.00 802.92
342.98 12064.00 803.64
342.98 13023.00 804.31
342.98 14042.00 805.0
342.98 15022.00 805.66
342.98 16022.00 806.36
342.98 17021.00 807.0
342.98 18034.00 807.7
342.98 19025.00 808.35
342.98 20038.00 808.98
342.98 21018.00 809.62
342.98 22035.00 810.28
352.86 1069.00 788.44
352.86 2043.00 789.24
352.86 3040.00 790.04
352.86 4048.00 790.78
352.86 5038.00 791.59
352.86 6043.00 792.34
352.86 7038.00 793.09
352.86 8039.00 793.84
352.86 9040.00 794.57
352.86 10038.00 795.32
352.86 11032.00 796.04
352.86 12032.00 796.74
352.86 13040.00 797.47
352.86 14046.00 798.18
352.86 15043.00 798.89
352.86 16037.00 799.59
352.86 17040.00 800.26
352.86 18046.00 800.95
352.86 19040.00 801.63
352.86 20064.00 802.32
352.86 21048.00 802.96
352.86 22049.00 803.62
362.89 1077.00 781.02
362.89 2027.00 781.83
362.89 3089.00 782.69
362.89 4047.00 783.49
362.89 5061.00 784.29
362.89 6060.00 785.12
362.89 7041.00 785.91
362.89 8049.00 786.7
362.89 9049.00 787.47
362.89 10052.00 788.25
362.89 11045.00 788.99
362.89 12044.00 789.75
362.89 13054.00 790.54
362.89 14053.00 791.25
362.89 15052.00 792.0
362.89 16056.00 792.77
362.89 17063.00 793.47
362.89 18062.00 794.2
362.89 19062.00 794.91
362.89 20068.00 795.64
362.89 21072.00 796.35
362.89 22063.00 797.03
Reference

Correlations

Property Value Unit Temperature (K) Source
Cp,gas [243.54; 621.86] J/mol×K [298.15; 1500.00] ChemSep v8.3 pure component data Show Hide
EquationY = A + B·((C/T)/sinh(C/T))² + D·((E/T)/cosh(E/T))²
Y is Cp,gas in J/mol×K, T in K
Coefficient A1.69840e+02
Coefficient B5.39200e+02
Coefficient C1.56800e+03
Coefficient D3.93800e+02
Coefficient E7.20500e+02
CommentChemSep eq 107, IdealGasHeatCapacityCp
Temperature range, min.298.15
Temperature range, max.1500.00
Cp,gas 243.54 J/mol×K 298.15 Calculated Property
Cp,gas 335.08 J/mol×K 431.69 Calculated Property
Cp,gas 407.02 J/mol×K 565.23 Calculated Property
Cp,gas 462.38 J/mol×K 698.77 Calculated Property
Cp,gas 505.99 J/mol×K 832.31 Calculated Property
Cp,gas 540.60 J/mol×K 965.84 Calculated Property
Cp,gas 568.10 J/mol×K 1099.38 Calculated Property
Cp,gas 590.04 J/mol×K 1232.92 Calculated Property
Cp,gas 607.64 J/mol×K 1366.46 Calculated Property
Cp,gas 621.86 J/mol×K 1500.00 Calculated Property
Property Value Unit Temperature (K) Source
Cp,liquid [353.69; 501.74] J/mol×K [280.00; 503.15] ChemSep v8.3 pure component data Show Hide
EquationY = A + B·T + C·T² + D·T³ + E·T⁴
Y is Cp,liquid in J/mol×K, T in K
Coefficient A4.98850e+03
Coefficient B-5.28980e+01
Coefficient C2.16350e-01
Coefficient D-3.75380e-04
Coefficient E2.36740e-07
CommentChemSep eq 100, LiquidHeatCapacityCp
Temperature range, min.280.00
Temperature range, max.503.15
Cp,liquid 353.69 J/mol×K 280.00 Calculated Property
Cp,liquid 378.47 J/mol×K 304.79 Calculated Property
Cp,liquid 409.66 J/mol×K 329.59 Calculated Property
Cp,liquid 440.40 J/mol×K 354.38 Calculated Property
Cp,liquid 465.98 J/mol×K 379.18 Calculated Property
Cp,liquid 483.82 J/mol×K 403.97 Calculated Property
Cp,liquid 493.52 J/mol×K 428.77 Calculated Property
Cp,liquid 496.79 J/mol×K 453.56 Calculated Property
Cp,liquid 497.53 J/mol×K 478.36 Calculated Property
Cp,liquid 501.74 J/mol×K 503.15 Calculated Property
Property Value Unit Temperature (K) Source
η [0.0193688; 0.0002727] Pa×s [285.00; 503.00] ChemSep v8.3 pure component data Show Hide
EquationY = exp(A + B/T + C·ln(T) + D·T^E)
Y is η in Pa×s, T in K
Coefficient A-6.99850e+01
Coefficient B5.81880e+03
Coefficient C8.07150e+00
Coefficient D0.00000e+00
Coefficient E0.00000e+00
CommentChemSep eq 101, LiquidViscosity
Temperature range, min.285.00
Temperature range, max.503.00
η 0.0193688 Pa×s 285.00 Calculated Property
η 0.0075591 Pa×s 309.22 Calculated Property
η 0.0035414 Pa×s 333.44 Calculated Property
η 0.0019131 Pa×s 357.67 Calculated Property
η 0.0011569 Pa×s 381.89 Calculated Property
η 0.0007659 Pa×s 406.11 Calculated Property
η 0.0005458 Pa×s 430.33 Calculated Property
η 0.0004131 Pa×s 454.56 Calculated Property
η 0.0003287 Pa×s 478.78 Calculated Property
η 0.0002727 Pa×s 503.00 Calculated Property
Property Value Unit Temperature (K) Source
ΔvapH [82.96; 0.00] kJ/mol [280.05; 688.00] ChemSep v8.3 pure component data 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 A7.90410e+01
Coefficient B-1.36000e+00
Coefficient C4.08540e+00
Coefficient D-2.38710e+00
Coefficient E0.00000e+00
Critical temperature, Tc (K)6.88000e+02
CommentChemSep eq 106, HeatOfVaporization
Temperature range, min.280.05
Temperature range, max.688.00
ΔvapH 82.96 kJ/mol 280.05 Calculated Property
ΔvapH 77.13 kJ/mol 325.38 Calculated Property
ΔvapH 70.47 kJ/mol 370.71 Calculated Property
ΔvapH 63.40 kJ/mol 416.03 Calculated Property
ΔvapH 56.26 kJ/mol 461.36 Calculated Property
ΔvapH 49.30 kJ/mol 506.69 Calculated Property
ΔvapH 42.60 kJ/mol 552.02 Calculated Property
ΔvapH 36.03 kJ/mol 597.34 Calculated Property
ΔvapH 28.63 kJ/mol 642.67 Calculated Property
ΔvapH 0.00 kJ/mol 688.00 Calculated Property
Property Value Unit Temperature (K) Source
Pvap [1.33; 202.67] kPa [390.26; 531.78] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.62798e+01
Coefficient B-4.94119e+03
Coefficient C-8.12810e+01
Temperature range, min.390.26
Temperature range, max.531.78
Pvap 1.33 kPa 390.26 Calculated Property
Pvap 2.89 kPa 405.98 Calculated Property
Pvap 5.84 kPa 421.71 Calculated Property
Pvap 11.09 kPa 437.43 Calculated Property
Pvap 19.94 kPa 453.16 Calculated Property
Pvap 34.18 kPa 468.88 Calculated Property
Pvap 56.19 kPa 484.61 Calculated Property
Pvap 88.98 kPa 500.33 Calculated Property
Pvap 136.30 kPa 516.06 Calculated Property
Pvap 202.67 kPa 531.78 Calculated Property
Pvap [1.51e-04; 2309.49] kPa [280.05; 688.00] ChemSep v8.3 pure component data Show Hide
EquationY = exp(A + B/T + C·ln(T) + D·T^E)
Y is Pvap in kPa, T in K
Coefficient A1.49332e+02
Coefficient B-1.52120e+04
Coefficient C-1.84240e+01
Coefficient D8.50060e-18
Coefficient E6.00000e+00
CommentChemSep eq 101, VaporPressure
Temperature range, min.280.05
Temperature range, max.688.00
Pvap 1.51e-04 kPa 280.05 Calculated Property
Pvap 0.02 kPa 325.38 Calculated Property
Pvap 0.51 kPa 370.71 Calculated Property
Pvap 5.48 kPa 416.03 Calculated Property
Pvap 30.76 kPa 461.36 Calculated Property
Pvap 111.16 kPa 506.69 Calculated Property
Pvap 297.16 kPa 552.02 Calculated Property
Pvap 650.07 kPa 597.34 Calculated Property
Pvap 1259.43 kPa 642.67 Calculated Property
Pvap 2309.49 kPa 688.00 Calculated Property
Pvap [1.20e-04; 2421.30] kPa [280.05; 690.00] 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 A2.35419e+02
Coefficient B-1.88148e+04
Coefficient C-3.16474e+01
Coefficient D1.36741e-05
Coefficient E0.00000e+00
Temperature range, min.280.05
Temperature range, max.690.00
Pvap 1.20e-04 kPa 280.05 Calculated Property
Pvap 0.02 kPa 325.60 Calculated Property
Pvap 0.53 kPa 371.15 Calculated Property
Pvap 5.66 kPa 416.70 Calculated Property
Pvap 31.38 kPa 462.25 Calculated Property
Pvap 112.99 kPa 507.80 Calculated Property
Pvap 304.78 kPa 553.35 Calculated Property
Pvap 678.49 kPa 598.90 Calculated Property
Pvap 1332.65 kPa 644.45 Calculated Property
Pvap 2421.30 kPa 690.00 Calculated Property
Pvap [0.12; 3.50] kPa [349.37; 406.18] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.50433e+01
Coefficient B-4.01201e+03
Coefficient C-1.15236e+02
ReferenceAmbrose, Ellender, et al., 1974
CommentCoefficents calculated by NIST from author's data.
Temperature range, min.349.37
Temperature range, max.406.18
Pvap 0.12 kPa 349.37 Calculated Property
Pvap 0.19 kPa 355.68 Calculated Property
Pvap 0.30 kPa 361.99 Calculated Property
Pvap 0.44 kPa 368.31 Calculated Property
Pvap 0.65 kPa 374.62 Calculated Property
Pvap 0.94 kPa 380.93 Calculated Property
Pvap 1.34 kPa 387.24 Calculated Property
Pvap 1.87 kPa 393.56 Calculated Property
Pvap 2.58 kPa 399.87 Calculated Property
Pvap 3.50 kPa 406.18 Calculated Property
Pvap [2.65; 177.80] kPa [400.41; 528.32] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.34874e+01
Coefficient B-3.16149e+03
Coefficient C-1.47727e+02
ReferenceAmbrose and Sprake, 1970
CommentCoefficents calculated by NIST from author's data.
Temperature range, min.400.41
Temperature range, max.528.32
Pvap 2.65 kPa 400.41 Calculated Property
Pvap 5.17 kPa 414.62 Calculated Property
Pvap 9.40 kPa 428.83 Calculated Property
Pvap 16.15 kPa 443.05 Calculated Property
Pvap 26.41 kPa 457.26 Calculated Property
Pvap 41.35 kPa 471.47 Calculated Property
Pvap 62.35 kPa 485.68 Calculated Property
Pvap 90.94 kPa 499.90 Calculated Property
Pvap 128.83 kPa 514.11 Calculated Property
Pvap 177.80 kPa 528.32 Calculated Property
Pvap [0.75; 99.35] kPa [378.00; 504.00] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.27073e+01
Coefficient B-2.71776e+03
Coefficient C-1.68829e+02
ReferenceKemme and Kreps, 1969
Temperature range, min.378.00
Temperature range, max.504.00
Pvap 0.75 kPa 378.00 Calculated Property
Pvap 1.70 kPa 392.00 Calculated Property
Pvap 3.48 kPa 406.00 Calculated Property
Pvap 6.60 kPa 420.00 Calculated Property
Pvap 11.68 kPa 434.00 Calculated Property
Pvap 19.53 kPa 448.00 Calculated Property
Pvap 31.10 kPa 462.00 Calculated Property
Pvap 47.44 kPa 476.00 Calculated Property
Pvap 69.77 kPa 490.00 Calculated Property
Pvap 99.35 kPa 504.00 Calculated Property
Property Value Unit Temperature (K) Source
ρl [832.71; 245.39] kg/m3 [280.05; 688.00] ChemSep v8.3 pure component data Show Hide
EquationY = A / B^(1 + (1 − T/C)^D)
Y is ρl in kg/m3, T in K
Coefficient A6.04760e+01
Coefficient B2.46450e-01
Coefficient C6.88000e+02
Coefficient D2.61250e-01
CommentChemSep eq 105, LiquidDensity
Temperature range, min.280.05
Temperature range, max.688.00
ρl 832.71 kg/m3 280.05 Calculated Property
ρl 802.44 kg/m3 325.38 Calculated Property
ρl 770.50 kg/m3 370.71 Calculated Property
ρl 736.47 kg/m3 416.03 Calculated Property
ρl 699.77 kg/m3 461.36 Calculated Property
ρl 659.45 kg/m3 506.69 Calculated Property
ρl 613.90 kg/m3 552.02 Calculated Property
ρl 559.85 kg/m3 597.34 Calculated Property
ρl 488.36 kg/m3 642.67 Calculated Property
ρl 245.39 kg/m3 688.00 Calculated Property
Property Value Unit Temperature (K) Source
γ [0.03; 0.00] N/m [280.05; 688.00] ChemSep v8.3 pure component data Show Hide
EquationY = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc
Y is γ in N/m, T in K
Coefficient A5.12630e-02
Coefficient B1.03950e+00
Coefficient C0.00000e+00
Coefficient D0.00000e+00
Coefficient E0.00000e+00
Critical temperature, Tc (K)6.88000e+02
CommentChemSep eq 106, SurfaceTension
Temperature range, min.280.05
Temperature range, max.688.00
γ 0.03 N/m 280.05 Calculated Property
γ 0.03 N/m 325.38 Calculated Property
γ 0.02 N/m 370.71 Calculated Property
γ 0.02 N/m 416.03 Calculated Property
γ 0.02 N/m 461.36 Calculated Property
γ 0.01 N/m 506.69 Calculated Property
γ 0.01 N/m 552.02 Calculated Property
γ 0.01 N/m 597.34 Calculated Property
γ 0.00 N/m 642.67 Calculated Property
γ 0.00 N/m 688.00 Calculated Property
Property Value Unit Temperature (K) Source
λ [0.03; 0.09] W/m×K [504.00; 1000.00] ChemSep v8.3 pure component data Show Hide
EquationY = A·T^B / (1 + C/T + D/T²)
Y is λ in W/m×K, T in K
Coefficient A-3.07200e-01
Coefficient B4.89000e-01
Coefficient C-6.75000e+04
Coefficient D-2.94000e+07
CommentChemSep eq 102, VaporThermalConductivity
Temperature range, min.504.00
Temperature range, max.1000.00
λ 0.03 W/m×K 504.00 Calculated Property
λ 0.03 W/m×K 559.11 Calculated Property
λ 0.04 W/m×K 614.22 Calculated Property
λ 0.04 W/m×K 669.33 Calculated Property
λ 0.05 W/m×K 724.44 Calculated Property
λ 0.06 W/m×K 779.56 Calculated Property
λ 0.07 W/m×K 834.67 Calculated Property
λ 0.08 W/m×K 889.78 Calculated Property
λ 0.08 W/m×K 944.89 Calculated Property
λ 0.09 W/m×K 1000.00 Calculated Property
Property Value Unit Temperature (K) Source
λ [0.17; 0.11] W/m×K [280.05; 503.00] ChemSep v8.3 pure component data Show Hide
EquationY = A + B·T + C·T² + D·T³ + E·T⁴
Y is λ in W/m×K, T in K
Coefficient A2.36170e-01
Coefficient B-2.50000e-04
Coefficient C0.00000e+00
Coefficient D0.00000e+00
Coefficient E0.00000e+00
CommentChemSep eq 100, LiquidThermalConductivity
Temperature range, min.280.05
Temperature range, max.503.00
λ 0.17 W/m×K 280.05 Calculated Property
λ 0.16 W/m×K 304.82 Calculated Property
λ 0.15 W/m×K 329.59 Calculated Property
λ 0.15 W/m×K 354.37 Calculated Property
λ 0.14 W/m×K 379.14 Calculated Property
λ 0.14 W/m×K 403.91 Calculated Property
λ 0.13 W/m×K 428.68 Calculated Property
λ 0.12 W/m×K 453.46 Calculated Property
λ 0.12 W/m×K 478.23 Calculated Property
λ 0.11 W/m×K 503.00 Calculated Property

Similar Compounds

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

Find more compounds similar to 1-Decanol.

Mixtures

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Sources

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