Chemical Properties of 1-Pentanol (CAS 71-41-0)

1-Pentanol

InChI
InChI=1S/C5H12O/c1-2-3-4-5-6/h6H,2-5H2,1H3
InChI Key
AMQJEAYHLZJPGS-UHFFFAOYSA-N
Formula
C5H12O
SMILES
CCCCCO
Molecular Weight1
88.15
CAS
71-41-0
Other Names
  • 1-Pentol
  • 1-Pentyl alcohol
  • Alcool amylique
  • Amyl alcohol, n-
  • Amyl alcohol, normal
  • Amylol
  • Butyl carbinol
  • NSC 5707
  • Pentanol
  • Pentanol-1
  • Pentasol
  • Primary amyl alcohol
  • Primary-N-amyl alcohol
  • UN 1105
  • amyl alcohol
  • n-Amylalkohol
  • n-Butylcarbinol
  • n-C5H11OH
  • n-Pentan-1-ol
  • n-Pentanol
  • n-amyl alcohol
  • n-pentyl alcohol
  • pentan-1-ol
  • pentyl 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 [0.5790; 0.5800]   Show Hide
ω 0.5800 PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω 0.5790 ChemSep v8.3 pure component data Compiled value
ω 0.5790 KDB
PAff 795.00 kJ/mol NIST
Tig [573.15; 633.15] K Show Hide
Tig 633.15 K KDB
Tig 573.15 K NCMS SOLV-DB
ΔcH°liquid [-3330.91; -3324.00] kJ/mol Show Hide
ΔcH°liquid -3330.91 ± 0.28 kJ/mol NIST
ΔcH°liquid -3329.90 ± 0.67 kJ/mol NIST
ΔcH°liquid -3329.96 ± 0.64 kJ/mol NIST
ΔcH°liquid -3324.60 ± 0.40 kJ/mol NIST
ΔcH°liquid -3324.00 kJ/mol NIST
Cp,liquid [206.67; 208.80] J/mol×K Show Hide
Cp,liquid 206.67 J/mol×K THERMODYNAMICS OF MIXTURES CONTAINING AMINES. XIV. CpEm OF BENZYLAMINE WITH HEPTANE AT 293.15 K OR WITH METHANOL, 1-PROPANOL OR 1-PENTANOL AT (293.15-308.15) K
Cp,liquid 208.80 J/mol×K Partial Molar Heat Capacities and Partial Molar Volumes of All of the Isomeric (C3 to C5) Alkanols at Infinite Dilution in Water at 298.15 K
μ [1.70; 1.70] debye Show Hide
μ 1.70 debye ChemSep v8.3 pure component data Compiled value
μ 1.70 debye KDB
εr 13.90 NCMS SOLV-DB
LFL 1.10 % in Air KDB
UFL 7.50 % in Air KDB
Tflash,cc 306.15 K NCMS SOLV-DB
Tflash,oc 298.15 K KDB
ΔfG° [-146.10; -146.02] kJ/mol Show Hide
ΔfG° -146.02 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfG° -146.10 kJ/mol KDB
ΔfH°gas [-301.00; -294.70] kJ/mol Show Hide
ΔfH°gas -300.16 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfH°gas -298.90 kJ/mol KDB
ΔfH°gas -294.70 kJ/mol NIST
ΔfH°gas -294.70 ± 0.30 kJ/mol NIST
ΔfH°gas -295.70 ± 0.70 kJ/mol NIST
ΔfH°gas -295.63 ± 0.74 kJ/mol NIST
ΔfH°gas -301.00 kJ/mol NIST
ΔfH°gas -301.00 ± 0.50 kJ/mol NIST
ΔfH°gas -300.60 ± 2.00 kJ/mol NIST
ΔfH°liquid [-358.40; -351.62] kJ/mol Show Hide
ΔfH°liquid -351.62 ± 0.28 kJ/mol NIST
ΔfH°liquid -352.60 ± 0.70 kJ/mol NIST
ΔfH°liquid -352.57 ± 0.72 kJ/mol NIST
ΔfH°liquid -357.90 ± 0.50 kJ/mol NIST
ΔfH°liquid -358.40 ± 1.70 kJ/mol NIST
ΔfusH° 10.51 kJ/mol Heat Capacities and Derived Thermodynamic Functions of 1-Propanol between 10 K and 350 K and of 1-Pentanol between 85 K and 370 K
ΔvapH° [54.23; 57.80] kJ/mol Show Hide
ΔvapH° 56.94 kJ/mol NCMS SOLV-DB
ΔvapH° 57.04 kJ/mol NIST
ΔvapH° Outlier 54.23 kJ/mol NIST
ΔvapH° 55.18 kJ/mol NIST
ΔvapH° 55.40 kJ/mol NIST
ΔvapH° 55.40 kJ/mol NIST
ΔvapH° 57.80 kJ/mol NIST
ΔvapH° 57.40 kJ/mol NIST
ΔvapH° 56.94 ± 0.17 kJ/mol NIST
ΔvapH° 56.90 kJ/mol NIST
ΔvapH° 56.90 ± 0.20 kJ/mol NIST
ΔvapH° 56.90 ± 0.20 kJ/mol NIST
ΔvapH° 57.70 ± 1.10 kJ/mol NIST
ΔvapH° 57.70 ± 1.00 kJ/mol NIST
ΔvapH° 57.80 kJ/mol NIST
IE [10.00; 10.42] eV Show Hide
IE 10.00 eV NIST
IE 10.38 eV NIST
IE 10.42 ± 0.03 eV NIST
log10WS [-0.60; -0.60]   Show Hide
log10WS -0.60 Aq. Solubility Prediction
log10WS -0.60 Estimated Solubility
logPoct/wat 1.560 NCMS SOLV-DB
McVol 87.180 ml/mol McGowan Calculated Property
NFPA Fire [%!d(float64=3); %!d(float64=3)]   Show Hide
NFPA Fire 3 KDB
NFPA Fire 3 NCMS SOLV-DB
NFPA Health [%!d(float64=1); %!d(float64=1)]   Show Hide
NFPA Health 1 KDB
NFPA Health 1 NCMS SOLV-DB
NFPA Safety 0 NCMS SOLV-DB
Pc [3850.35; 3920.00] kPa Show Hide
Pc 3897.00 kPa IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Pc 3850.35 kPa PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc 3909.00 kPa ChemSep v8.3 pure component data Compiled value
Pc 3897.00 kPa KDB
Pc 3900.00 ± 20.00 kPa NIST
Pc 3920.00 ± 40.00 kPa NIST
Pc 3868.00 ± 20.00 kPa NIST
Pc 3868.00 ± 20.00 kPa NIST
Pc 3909.00 kPa NIST
Pc 3909.00 kPa NIST
Ptriple 3.45e-07 kPa ChemSep v8.3 pure component data Compiled value
ρc [269.73; 273.26] kg/m3 Show Hide
ρc 269.73 ± 1.76 kg/m3 NIST
ρc 269.73 kg/m3 NIST
ρc 273.26 ± 17.63 kg/m3 NIST
Inp [722.00; 801.00]   Show Hide
Inp 754.00 NIST
Inp 762.00 NIST
Inp 749.00 NIST
Inp 765.00 NIST
Inp 766.00 NIST
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Inp 745.00 NIST
Inp 759.00 NIST
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Inp 764.00 NIST
Inp 781.00 NIST
Inp 744.00 NIST
Inp 740.00 NIST
Inp 761.00 NIST
Inp 767.00 NIST
Inp Outlier 791.40 NIST
Inp Outlier 793.10 NIST
Inp 775.50 NIST
Inp 771.90 NIST
Inp 766.50 NIST
Inp 762.30 NIST
Inp 757.90 NIST
Inp 757.18 NIST
Inp 754.60 NIST
Inp 753.50 NIST
Inp 752.70 NIST
Inp 752.20 NIST
Inp 766.00 NIST
Inp 763.40 NIST
Inp 761.50 NIST
Inp 754.60 NIST
Inp 753.50 NIST
Inp 752.70 NIST
Inp 752.20 NIST
Inp 766.00 NIST
Inp 763.40 NIST
Inp 761.50 NIST
Inp Outlier 730.20 NIST
Inp 734.70 NIST
Inp 754.00 NIST
Inp 748.00 NIST
Inp 768.00 NIST
Inp 760.00 NIST
Inp 749.00 NIST
Inp 754.00 NIST
Inp Outlier 789.00 NIST
Inp 746.40 NIST
Inp 742.00 NIST
Inp Outlier 728.00 NIST
Inp Outlier 731.00 NIST
Inp Outlier 730.00 NIST
Inp 751.00 NIST
Inp 747.00 NIST
Inp 746.00 NIST
Inp 736.00 NIST
Inp 746.00 NIST
Inp Outlier 730.00 NIST
Inp Outlier 722.00 NIST
Inp 752.00 NIST
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Inp 744.10 NIST
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Inp 783.00 NIST
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Inp 749.00 NIST
Inp 748.30 NIST
Inp 752.00 NIST
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Inp 768.00 NIST
Inp 751.90 NIST
Inp 751.90 NIST
Inp 764.00 NIST
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Inp 758.00 NIST
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Inp 771.00 NIST
Inp 780.00 NIST
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Inp 768.00 NIST
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Inp Outlier 800.00 NIST
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Inp Outlier 801.00 NIST
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Inp Outlier 787.00 NIST
Inp Outlier 730.00 NIST
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Inp 750.00 NIST
Inp Outlier 723.00 NIST
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Ip [1200.00; 1294.00]   Show Hide
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Ip Outlier 1206.00 NIST
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Ip Outlier 1288.00 NIST
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Ip Outlier 1213.00 NIST
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S°gas 401.30 J/mol×K NIST
S°liquid [254.80; 258.90] J/mol×K Show Hide
S°liquid 258.90 J/mol×K NIST
S°liquid 254.80 J/mol×K NIST
Tboil [273.28; 684.20] K Show Hide
Tboil 411.15 K Excess molar volumes of ternary mixtures of 1,3-dichlorobenzene and methyl ethyl ketone with 1-alkanols at 303.15K
Tboil 410.95 K Liquid-liquid equilibrium data for ternary aqueous mixtures containing 1-pentanol and 2-methyl-1-propanol at (298.15, 323.15, and 348.15) K
Tboil 411.11 K Isobaric Phase Equilibria of Diethyl Carbonate with Five Alcohols at 101.3 kPa
Tboil 410.78 K Vapor-Liquid Equilibria of the Binary System 1-Pentanol + Anisole and the Quaternary System Benzene+Cyclohexane+1-Pentanol+Anisole at 101.32 kPa
Tboil 410.85 K Vapor-Liquid Equilibria at 101.3 kPa for Binary Mixtures Containing 2-Methyl-1-propanol + 2-Methyl-1-butanol, 2-Methyl-1-propanol + 3-Methyl-1-butanol, and 2-Methyl-1-propanol + 1-Pentanol
Tboil 411.10 K Isobaric Vapor-Liquid Equilibria of Heptane + 1-Butanol and Heptane + 1-Pentanol Systems at (53.3 and 91.3) kPa
Tboil 411.16 K ChemSep v8.3 pure component data Compiled value
Tboil 411.13 K KDB
Tboil 411.13 K NCMS SOLV-DB
Tboil Outlier 684.20 ± 0.40 K NIST
Tboil 410.90 ± 0.30 K NIST
Tboil 410.20 K NIST
Tboil 410.15 ± 0.40 K NIST
Tboil 411.20 K NIST
Tboil 392.40 K NIST
Tboil 411.00 ± 0.30 K NIST
Tboil 411.10 ± 0.08 K NIST
Tboil 411.00 ± 0.50 K NIST
Tboil Outlier 273.28 ± 0.10 K NIST
Tboil 410.80 ± 0.40 K NIST
Tboil 411.20 ± 0.50 K NIST
Tboil 411.20 ± 0.40 K NIST
Tboil 411.15 K NIST
Tboil 409.15 ± 3.00 K NIST
Tboil 411.65 ± 0.50 K NIST
Tboil 410.65 ± 3.00 K NIST
Tboil 410.65 ± 0.50 K NIST
Tboil 411.15 ± 0.50 K NIST
Tboil 411.00 ± 0.50 K NIST
Tboil 410.15 ± 0.70 K NIST
Tboil 408.65 ± 2.00 K NIST
Tboil 411.07 ± 0.20 K NIST
Tboil 409.65 ± 1.00 K NIST
Tboil 406.65 ± 3.00 K NIST
Tboil 410.65 ± 0.50 K NIST
Tboil 411.15 ± 0.50 K NIST
Tboil 411.35 ± 0.50 K NIST
Tboil 411.05 ± 1.00 K NIST
Tboil 411.15 ± 0.50 K NIST
Tboil 410.15 ± 1.00 K NIST
Tboil 410.15 ± 1.00 K NIST
Tboil 411.40 ± 0.50 K NIST
Tboil 411.35 ± 0.50 K NIST
Tboil 411.15 ± 0.50 K NIST
Tboil 409.15 ± 3.00 K NIST
Tboil 410.90 ± 0.50 K NIST
Tboil 411.15 ± 1.00 K NIST
Tboil 410.95 ± 0.50 K NIST
Tboil 411.10 ± 0.50 K NIST
Tboil 407.15 ± 3.00 K NIST
Tboil 411.21 ± 0.05 K NIST
Tboil 410.80 ± 0.20 K NIST
Tboil 411.10 ± 0.10 K NIST
Tboil 409.85 ± 0.50 K NIST
Tboil 410.95 ± 0.30 K NIST
Tboil 411.40 ± 0.10 K NIST
Tboil 408.90 ± 1.50 K NIST
Tboil 410.95 ± 0.30 K NIST
Tboil 410.95 ± 0.50 K NIST
Tboil 411.15 ± 0.07 K NIST
Tboil 410.40 ± 0.30 K NIST
Tboil 409.15 ± 2.00 K NIST
Tboil 411.20 ± 0.20 K NIST
Tboil 411.00 ± 0.50 K NIST
Tboil 410.65 ± 1.00 K NIST
Tboil 411.15 ± 1.00 K NIST
Tboil 411.10 ± 0.20 K NIST
Tboil 411.10 ± 0.10 K NIST
Tboil 402.20 ± 0.50 K NIST
Tboil 404.15 ± 4.00 K NIST
Tboil 410.00 ± 3.00 K NIST
Tboil 404.75 ± 3.00 K NIST
Tboil 411.00 ± 1.00 K NIST
Tboil 402.90 ± 1.00 K NIST
Tboil 404.15 ± 3.00 K NIST
Tboil 404.25 ± 3.00 K NIST
Tc [551.60; 588.50] K Show Hide
Tc 588.10 K IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Tc 586.00 K PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc 588.15 K ChemSep v8.3 pure component data Compiled value
Tc 588.10 K KDB
Tc 588.10 ± 0.50 K NIST
Tc 588.00 ± 0.40 K NIST
Tc 588.20 ± 0.50 K NIST
Tc 588.50 ± 0.60 K NIST
Tc 588.50 ± 0.60 K NIST
Tc 588.00 K NIST
Tc 587.70 ± 0.20 K NIST
Tc 588.20 K NIST
Tc Outlier 551.60 K NIST
Tc 588.11 K NIST
Tfus [194.20; 194.95] K Show Hide
Tfus 194.70 K Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus 194.95 K ChemSep v8.3 pure component data Compiled value
Tfus 194.20 K KDB
Tfus 194.68 K Aq. Solubility Prediction
Tfus 194.95 K NCMS SOLV-DB
Tfus 194.95 K NIST
Tfus 194.35 ± 0.30 K NIST
Tfus 194.65 ± 0.50 K NIST
Tfus 194.65 ± 0.50 K NIST
Ttriple [194.20; 195.56] K Show Hide
Ttriple 195.56 K ChemSep v8.3 pure component data Compiled value
Ttriple 195.56 K KDB
Ttriple 195.56 ± 0.02 K NIST
Ttriple 194.20 ± 0.20 K NIST
Ttriple 195.56 ± 0.02 K NIST
Ttriple 194.20 ± 0.20 K NIST
UQi 4.21 ChemSep v8.3 pure component data Compiled value
URi 4.60 ChemSep v8.3 pure component data Compiled value
Vc [0.326; 0.326] m3/kmol Show Hide
Vc 0.326 m3/kmol IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Vc 0.326 m3/kmol PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc 0.326 m3/kmol ChemSep v8.3 pure component data Compiled value
Vc 0.326 m3/kmol KDB
Vc 0.326 m3/kmol NIST
Zc [0.2598130; 0.2620000]   Show Hide
Zc 0.2600000 IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Zc 0.2620000 ChemSep v8.3 pure component data Compiled value
Zc 0.2598130 KDB
Zra [0.26; 0.26]   Show Hide
Zra 0.26 ChemSep v8.3 pure component data Compiled value
Zra 0.26 KDB

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,gas [167.91; 221.40] J/mol×K [403.49; 573.95] Show Hide
Cp,gas 167.91 J/mol×K 403.49 NIST
Cp,gas 177.70 ± 1.40 J/mol×K 418.95 NIST
Cp,gas 178.20 ± 1.40 J/mol×K 420.75 NIST
Cp,gas 174.58 J/mol×K 423.32 NIST
Cp,gas 179.70 ± 1.40 J/mol×K 426.15 NIST
Cp,gas 181.70 ± 1.40 J/mol×K 433.45 NIST
Cp,gas 179.33 J/mol×K 438.26 NIST
Cp,gas 184.40 ± 1.40 J/mol×K 442.85 NIST
Cp,gas 184.80 ± 1.40 J/mol×K 444.35 NIST
Cp,gas 184.35 J/mol×K 453.45 NIST
Cp,gas 192.90 ± 1.40 J/mol×K 472.85 NIST
Cp,gas 190.44 J/mol×K 473.19 NIST
Cp,gas 195.50 ± 1.40 J/mol×K 482.25 NIST
Cp,gas 209.30 ± 1.40 J/mol×K 531.25 NIST
Cp,gas 215.80 ± 1.40 J/mol×K 554.15 NIST
Cp,gas 221.40 ± 1.40 J/mol×K 573.95 NIST
Cp,liquid [183.30; 240.60] J/mol×K [293.15; 313.20] Show Hide
Cp,liquid 205.60 J/mol×K 293.15 NIST
Cp,liquid 183.30 J/mol×K 298.00 NIST
Cp,liquid 209.12 J/mol×K 298.00 NIST
Cp,liquid 208.30 J/mol×K 298.15 NIST
Cp,liquid 207.40 J/mol×K 298.15 NIST
Cp,liquid 208.98 J/mol×K 298.15 NIST
Cp,liquid 208.40 J/mol×K 298.15 NIST
Cp,liquid 207.45 J/mol×K 298.15 NIST
Cp,liquid 208.19 J/mol×K 298.15 NIST
Cp,liquid 207.45 J/mol×K 298.15 NIST
Cp,liquid 212.30 J/mol×K 301.26 NIST
Cp,liquid 201.70 J/mol×K 302.40 NIST
Cp,liquid 240.60 J/mol×K 313.20 NIST
η [0.0006470; 0.0054170] Pa×s [283.15; 373.15] Show Hide
η 0.0054170 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 0.0046820 Pa×s 288.15 Densities and Viscosities of Four Binary Diethyl Carbonate + 1-Alcohol Systems from (288.15 to 313.15) K
η 0.0040250 Pa×s 293.15 Densities and Viscosities of Four Binary Diethyl Carbonate + 1-Alcohol Systems from (288.15 to 313.15) K
η 0.0040300 Pa×s 293.15 Density, viscosity, vapour liquid equilibrium, excess molar enthalpy, and their correlations of the binary system [1-pentanol + R-(+)-limonene] over the complete concentration range, at different temperatures
η 0.0039740 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 0.0041170 Pa×s 293.15 Density and Viscosity of Binary Mixtures of Diethyl Carbonate with Alcohols at (293.15 to 363.15) K and Predictive Results by UNIFAC-VISCO Group Contribution Method
η 0.0040601 Pa×s 293.15 Densities and Viscosities of exo-Tetrahydrodicyclopentadiene + n-Butanol and exo-Tetrahydrodicyclopentadiene + n-Pentanol at Temperatures of (293.15 to 313.15) K
η 0.0040290 Pa×s 293.15 Densities and Kinematic Viscosities of Ten Binary 1-Alkanol Liquid Systems at Temperatures of (293.15 and 298.15) K
η 0.0034940 Pa×s 298.15 Densities and Kinematic Viscosities of Ten Binary 1-Alkanol Liquid Systems at Temperatures of (293.15 and 298.15) K
η 0.0034970 Pa×s 298.15 Densities and Viscosities of Four Binary Diethyl Carbonate + 1-Alcohol Systems from (288.15 to 313.15) K
η 0.0035344 Pa×s 298.15 Densities and Viscosities of exo-Tetrahydrodicyclopentadiene + n-Butanol and exo-Tetrahydrodicyclopentadiene + n-Pentanol at Temperatures of (293.15 to 313.15) K
η 0.0035560 Pa×s 298.15 Density and Viscosity of Binary Mixtures of Diethyl Carbonate with Alcohols at (293.15 to 363.15) K and Predictive Results by UNIFAC-VISCO Group Contribution Method
η 0.0034580 Pa×s 298.15 Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
η 0.0034410 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 0.0035120 Pa×s 298.15 NCMS SOLV-DB
η 0.0034800 Pa×s 298.15 Density, viscosity, vapour liquid equilibrium, excess molar enthalpy, and their correlations of the binary system [1-pentanol + R-(+)-limonene] over the complete concentration range, at different temperatures
η 0.0030070 Pa×s 303.15 Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
η 0.0030220 Pa×s 303.15 Densities and Viscosities of Four Binary Diethyl Carbonate + 1-Alcohol Systems from (288.15 to 313.15) K
η 0.0030582 Pa×s 303.15 Densities and Viscosities of exo-Tetrahydrodicyclopentadiene + n-Butanol and exo-Tetrahydrodicyclopentadiene + n-Pentanol at Temperatures of (293.15 to 313.15) K
η 0.0030200 Pa×s 303.15 Density, viscosity, vapour liquid equilibrium, excess molar enthalpy, and their correlations of the binary system [1-pentanol + R-(+)-limonene] over the complete concentration range, at different temperatures
η 0.0030600 Pa×s 303.15 Density and Viscosity of Binary Mixtures of Diethyl Carbonate with Alcohols at (293.15 to 363.15) K and Predictive Results by UNIFAC-VISCO Group Contribution Method
η 0.0029900 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 0.0026250 Pa×s 308.15 Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
η 0.0023120 Pa×s 313.15 Densities and Viscosities of Four Binary Diethyl Carbonate + 1-Alcohol Systems from (288.15 to 313.15) K
η 0.0023170 Pa×s 313.15 Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
η 0.0022995 Pa×s 313.15 Densities and Viscosities of exo-Tetrahydrodicyclopentadiene + n-Butanol and exo-Tetrahydrodicyclopentadiene + n-Pentanol at Temperatures of (293.15 to 313.15) K
η 0.0023320 Pa×s 313.15 Density and Viscosity of Binary Mixtures of Diethyl Carbonate with Alcohols at (293.15 to 363.15) K and Predictive Results by UNIFAC-VISCO Group Contribution Method
η 0.0023150 Pa×s 313.15 Density, viscosity, vapour liquid equilibrium, excess molar enthalpy, and their correlations of the binary system [1-pentanol + R-(+)-limonene] over the complete concentration range, at different temperatures
η 0.0022630 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 0.0020290 Pa×s 318.15 Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
η 0.0018010 Pa×s 323.15 Density, viscosity, vapour liquid equilibrium, excess molar enthalpy, and their correlations of the binary system [1-pentanol + R-(+)-limonene] over the complete concentration range, at different temperatures
η 0.0018220 Pa×s 323.15 Density and Viscosity of Binary Mixtures of Diethyl Carbonate with Alcohols at (293.15 to 363.15) K and Predictive Results by UNIFAC-VISCO Group Contribution Method
η 0.0017950 Pa×s 323.15 Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
η 0.0014250 Pa×s 333.15 Density, viscosity, vapour liquid equilibrium, excess molar enthalpy, and their correlations of the binary system [1-pentanol + R-(+)-limonene] over the complete concentration range, at different temperatures
η 0.0014400 Pa×s 333.15 Density and Viscosity of Binary Mixtures of Diethyl Carbonate with Alcohols at (293.15 to 363.15) K and Predictive Results by UNIFAC-VISCO Group Contribution Method
η 0.0011460 Pa×s 343.15 Density, viscosity, vapour liquid equilibrium, excess molar enthalpy, and their correlations of the binary system [1-pentanol + R-(+)-limonene] over the complete concentration range, at different temperatures
η 0.0011460 Pa×s 343.15 Density and Viscosity of Binary Mixtures of Diethyl Carbonate with Alcohols at (293.15 to 363.15) K and Predictive Results by UNIFAC-VISCO Group Contribution Method
η 0.0009350 Pa×s 353.15 Density, viscosity, vapour liquid equilibrium, excess molar enthalpy, and their correlations of the binary system [1-pentanol + R-(+)-limonene] over the complete concentration range, at different temperatures
η 0.0009310 Pa×s 353.15 Density and Viscosity of Binary Mixtures of Diethyl Carbonate with Alcohols at (293.15 to 363.15) K and Predictive Results by UNIFAC-VISCO Group Contribution Method
η 0.0007720 Pa×s 363.15 Density, viscosity, vapour liquid equilibrium, excess molar enthalpy, and their correlations of the binary system [1-pentanol + R-(+)-limonene] over the complete concentration range, at different temperatures
η 0.0007670 Pa×s 363.15 Density and Viscosity of Binary Mixtures of Diethyl Carbonate with Alcohols at (293.15 to 363.15) K and Predictive Results by UNIFAC-VISCO Group Contribution Method
η 0.0006470 Pa×s 373.15 Density, viscosity, vapour liquid equilibrium, excess molar enthalpy, and their correlations of the binary system [1-pentanol + R-(+)-limonene] over the complete concentration range, at different temperatures
ΔfusH [9.83; 10.51] kJ/mol [194.20; 195.60] Show Hide
ΔfusH 9.83 kJ/mol 194.20 NIST
ΔfusH 9.83 kJ/mol 194.20 NIST
ΔfusH 10.50 kJ/mol 195.56 NIST
ΔfusH 10.50 kJ/mol 195.56 NIST
ΔfusH 10.51 kJ/mol 195.60 NIST
ΔfusH 10.50 kJ/mol 195.60 NIST
ΔfusH 10.50 kJ/mol 195.60 NIST
ΔvapH [7.10; 56.20] kJ/mol [313.00; 586.00] Show Hide
ΔvapH 55.70 ± 0.20 kJ/mol 313.00 NIST
ΔvapH 54.40 ± 0.20 kJ/mol 328.00 NIST
ΔvapH 53.00 ± 0.20 kJ/mol 343.00 NIST
ΔvapH 51.20 ± 0.20 kJ/mol 358.00 NIST
ΔvapH 56.20 kJ/mol 359.00 NIST
ΔvapH 55.00 kJ/mol 360.50 NIST
ΔvapH 50.50 ± 0.10 kJ/mol 362.00 NIST
ΔvapH 54.30 kJ/mol 368.50 NIST
ΔvapH 51.50 kJ/mol 372.50 NIST
ΔvapH 49.20 ± 0.10 kJ/mol 374.00 NIST
ΔvapH 51.60 kJ/mol 388.00 NIST
ΔvapH 47.00 ± 0.10 kJ/mol 392.00 NIST
ΔvapH 41.40 kJ/mol 392.40 NIST
ΔvapH 47.20 kJ/mol 404.00 NIST
ΔvapH 44.35 kJ/mol 410.90 KDB
ΔvapH 44.40 kJ/mol 411.00 NIST
ΔvapH 44.40 ± 0.10 kJ/mol 411.00 NIST
ΔvapH 44.36 kJ/mol 411.20 NIST
ΔvapH 45.40 kJ/mol 424.50 NIST
ΔvapH 40.10 kJ/mol 448.00 NIST
ΔvapH 36.10 kJ/mol 473.00 NIST
ΔvapH 31.70 kJ/mol 498.00 NIST
ΔvapH 26.40 kJ/mol 523.00 NIST
ΔvapH 22.00 kJ/mol 548.00 NIST
ΔvapH 14.10 kJ/mol 573.00 NIST
ΔvapH 7.10 kJ/mol 586.00 NIST
ν [0.0000029; 0.0000050] m2/s [293.15; 313.15] Show Hide
ν 0.0000050 m2/s 293.15 Densities, Viscosities, and Speeds of Sound of the Nitromethane + 1-Pentanol System near the Critical Demixing Temperature: Effect of Deuterium Substitution
ν 0.0000044 m2/s 295.15 Densities, Viscosities, and Speeds of Sound of the Nitromethane + 1-Pentanol System near the Critical Demixing Temperature: Effect of Deuterium Substitution
ν 0.0000042 m2/s 298.15 Densities, Viscosities, and Speeds of Sound of the Nitromethane + 1-Pentanol System near the Critical Demixing Temperature: Effect of Deuterium Substitution
ν 0.0000039 m2/s 300.15 Densities, Viscosities, and Speeds of Sound of the Nitromethane + 1-Pentanol System near the Critical Demixing Temperature: Effect of Deuterium Substitution
ν 0.0000036 m2/s 303.15 Densities, Viscosities, and Speeds of Sound of the Nitromethane + 1-Pentanol System near the Critical Demixing Temperature: Effect of Deuterium Substitution
ν 0.0000037 m2/s 303.15 Densities, Viscosities, and Ultrasonic Velocity Studies of Binary Mixtures of Chloroform with Pentan-1-ol, Hexan-1-ol, and Heptan-1-ol at (303.15 and 313.15) K
ν 0.0000035 m2/s 305.15 Densities, Viscosities, and Speeds of Sound of the Nitromethane + 1-Pentanol System near the Critical Demixing Temperature: Effect of Deuterium Substitution
ν 0.0000031 m2/s 308.15 Densities, Viscosities, and Speeds of Sound of the Nitromethane + 1-Pentanol System near the Critical Demixing Temperature: Effect of Deuterium Substitution
ν 0.0000029 m2/s 313.15 Densities, Viscosities, and Ultrasonic Velocity Studies of Binary Mixtures of Chloroform with Pentan-1-ol, Hexan-1-ol, and Heptan-1-ol at (303.15 and 313.15) K
Pvap [0.29; 113.30] kPa [298.15; 414.65] Show Hide
Pvap 0.34 kPa 298.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 0.29 kPa 298.15 NCMS SOLV-DB
Pvap 0.49 kPa 303.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 0.69 kPa 308.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 0.91 kPa 313.15 Characterizing second generation biofuels: Excess enthalpies and vapour-liquid equilibria of the binary mixtures containing 1-pentanol or 2-pentanol and n-hexane
Pvap 0.90 kPa 313.15 Vapour-liquid equilibria of the ternary mixture (1-pentanol + 2,2,4-trimethylpentane + heptane) and the binary mixture (2,2,4-trimethylpentane + heptane) at T = 313.15 K for the characterization of second generation biofuels.
Pvap 0.97 kPa 313.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 1.36 kPa 318.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 1.87 kPa 323.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 2.53 kPa 328.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 3.38 kPa 333.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 4.47 kPa 338.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 5.87 kPa 343.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 7.63 kPa 348.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 9.83 kPa 353.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 12.52 kPa 358.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 15.81 kPa 363.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 19.86 kPa 368.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 24.68 kPa 373.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 30.47 kPa 378.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 31.30 kPa 379.35 Isobaric (vapour + liquid) equilibria for the (1-pentanol + propionic acid) binary mixture at (53.3 and 91.3) kPa
Pvap 35.30 kPa 382.40 Isobaric (vapour + liquid) equilibria for the (1-pentanol + propionic acid) binary mixture at (53.3 and 91.3) kPa
Pvap 37.36 kPa 383.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 40.00 kPa 384.45 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 40.01 kPa 384.85 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 40.00 kPa 385.65 Isobaric (vapour + liquid) equilibria for the (1-pentanol + propionic acid) binary mixture at (53.3 and 91.3) kPa
Pvap 45.45 kPa 388.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 49.20 kPa 390.75 Isobaric (vapour + liquid) equilibria for the (1-pentanol + propionic acid) binary mixture at (53.3 and 91.3) kPa
Pvap 54.41 kPa 392.76 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 54.88 kPa 393.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 56.90 kPa 394.70 Isobaric (vapour + liquid) equilibria for the (1-pentanol + propionic acid) binary mixture at (53.3 and 91.3) kPa
Pvap 66.15 kPa 398.11 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 65.84 kPa 398.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 69.30 kPa 400.05 Isobaric (vapour + liquid) equilibria for the (1-pentanol + propionic acid) binary mixture at (53.3 and 91.3) kPa
Pvap 72.93 kPa 400.95 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 78.45 kPa 403.15 Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 82.75 kPa 404.59 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 81.30 kPa 404.60 Isobaric (vapour + liquid) equilibria for the (1-pentanol + propionic acid) binary mixture at (53.3 and 91.3) kPa
Pvap 90.21 kPa 407.17 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 94.50 kPa 409.00 Isobaric (vapour + liquid) equilibria for the (1-pentanol + propionic acid) binary mixture at (53.3 and 91.3) kPa
Pvap 101.20 kPa 410.73 Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 101.90 kPa 411.35 Isobaric (vapour + liquid) equilibria for the (1-pentanol + propionic acid) binary mixture at (53.3 and 91.3) kPa
Pvap 113.30 kPa 414.65 Isobaric (vapour + liquid) equilibria for the (1-pentanol + propionic acid) binary mixture at (53.3 and 91.3) kPa
n0 [1.39776; 1.41192]   [288.15; 323.15] Show Hide
n0 1.41192 288.15 Experimental Determination and Modeling of Densities and Refractive Indices of the Binary Systems Alcohol + Dicyclohexylamine at T = (288.15 to 323.15) K
n0 1.41040 293.00 Quaternary Liquid-Liquid Equilibrium of Water + Acetic Acid + Propionic Acid + Solvent (Amyl Alcohol, Cyclohexyl Acetate, or Toluene) Systems
n0 1.40900 293.10 Viscosity and surface tension of binary systems of N,N-dimethylformamide with alkan-1-ols at different temperatures
n0 1.40980 293.13 Isobaric Vapor-Liquid Equilibria of the Ternary System Pentan-1-ol + Pentyl Acetate + Nonane
n0 1.40980 293.13 Isobaric Vapor-Liquid Equilibria of the Ternary System Methylbutyl Ketone + 1-Pentanol + Anisole
n0 1.41001 293.15 DIELECTRIC AND REFRACTIVE INDEX MEASUREMENTS FOR THE SYSTEMS 1-PENTANOL + OCTANE, OR + DIBUTYL ETHER OR FOR DIBUTYL ETHER + OCTANE AT DIFFERENT TEMPERATURES
n0 1.40994 293.15 Experimental Determination and Modeling of Densities and Refractive Indices of the Binary Systems Alcohol + Dicyclohexylamine at T = (288.15 to 323.15) K
n0 1.41000 293.15 Isothermal Vapor-Liquid Equilibrium Measurements of Butan-2-one + 2-Methyl-propan-1-ol/Pentan-1-ol
n0 1.40976 293.15 Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrachloroethane and 1-alkanols binary mixtures
n0 1.41000 293.15 DIELECTRIC AND REFRACTIVE INDEX MEASUREMENTS FOR THE SYSTEMS 1-PENTANOL + 2,5,8,11,14-PENTAOXAPENTADECANE, OR FOR 2,5,8,11,14-PENTAOXAPENTADECANE + OCTANE AT (293.15-303.15) K.
n0 1.40980 293.15 Isobaric Vapor-Liquid Equilibria of the Ternary System Methylbutyl Ketone + 1-Pentanol + Nonane
n0 1.40920 293.15 Measurement and Correlation of the Solubilities of m-Phthalic Acid in Monobasic Alcohols
n0 1.40980 293.15 Isobaric Vapor-Liquid Equilibria of the Ternary System Dibutyl Ether + 1-Pentanol + Nonane
n0 1.40995 293.15 Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrabromoethane and 1-alkanols binary mixtures
n0 1.40980 293.15 Isobaric Vapor Liquid Equilibria of the Ternary System 1-Pentanol + Nonane Anisole
n0 1.40995 293.15 Excess molar volumes and viscosities of (1,1,2,2-tetrabromoethane + 1-alkanols) at T = (293.15 and 303.15) K
n0 1.40980 293.15 Experimental solubility for betulin and estrone in various solvents within the temperature range T = (293.2 to 328.2) K
n0 1.40980 293.15 ERAS modeling of the excess molar enthalpies of binary liquid mixtures of 1-pentanol and 1-hexanol with acetonitrile at atmospheric pressure and 288, 298, 313 and 323K
n0 1.41000 293.20 Liquid-liquid equilibrium data for systems containing of formic acid, water, and primary normal alcohols at T = 298.2 K
n0 1.40970 293.20 Vapor Liquid Equilibrium Data for Binary Systems of 1H-Pyrrole with Butan-1-ol, Propan-1-ol, or Pentan-1-ol
n0 1.40970 293.20 Vapor Liquid Equilibrium Data for Binary Systems of 1-Methyl-4-(1-methylethenyl)-cyclohexene + {Ethanol, Propan-1-ol, Propan-2-ol, Butan-1-ol, Pentan-1-ol, or Hexan-1-ol} at 40 kPa
n0 1.40820 298.15 DIELECTRIC AND REFRACTIVE INDEX MEASUREMENTS FOR THE SYSTEMS 1-PENTANOL + 2,5,8,11,14-PENTAOXAPENTADECANE, OR FOR 2,5,8,11,14-PENTAOXAPENTADECANE + OCTANE AT (293.15-303.15) K.
n0 1.40730 298.15 Thermodynamic properties of (tetradecane + benzene, + toluene, + chlorobenzene, + bromobenzene, + anisole) binary mixtures at T = (298.15, 303.15, and 308.15) K
n0 1.40770 298.15 Isobaric Vapor Liquid Equilibrium of 3-Methyl-1-butanol + Ethyl Lactate and 1-Pentanol + Ethyl Lactate at (13.0 and 101.3) kPa
n0 1.40770 298.15 Isobaric Vapor-Liquid Equilibrium for Binary Mixtures of 3-Methyl-1-butanol + 3-Methyl-1-butyl Ethanoate and 1-Pentanol + Pentyl Ethanoate at 101.3 kPa
n0 1.40784 298.15 Thermophysical properties of the binary mixtures (1,8-cineole + 1-alkanol) at T = (298.15 and 313.15) K and at atmospheric pressure
n0 1.40680 298.15 Densities, Viscosities, and Refractive Indices of Binary Mixtures of Methyl Ethyl Ketone + Pentanol Isomers at Different Temperatures
n0 1.40780 298.15 Excess molar volumes, excess molar enthalpies and refractive index deviations for binary mixtures of propan-1-ol, butan-1-ol and pentan-1-ol with 2,2,4-trimethylpentane at 298.15 K
n0 1.40774 298.15 Effect of the temperature on the physical properties of the pure ionic liquid 1-ethyl-3-methylimidazolium methylsulfate and characterization of its binary mixtures with alcohols
n0 1.40780 298.15 Mixing thermodynamic properties of 1-butyl-4-methylpyridinium tetrafluoroborate [b4mpy][BF4] with water and with an alkan-1ol (methanol to pentanol)
n0 1.40710 298.15 Liquid-liquid equilibrium for (water + 5-hydroxymethylfurfural + 1-pentanol/1-hexanol/1-heptanol) systems at 298.15 K
n0 1.40800 298.15 Vapor liquid equilibria in the ternary system dipropyl ether + 1-propanol + 1-pentanol and the binary systems dipropyl ether + 1-pentanol, 1-propanol + 1-pentanol at 101.3 kPa
n0 1.40860 298.15 Excess Molar Enthalpies of 2-Methyl-2-butanol (1) + 1-Alkanols (C1-C5) (2) at 298.15 K
n0 1.40730 298.15 Thermodynamic interactions in binary mixtures of anisole with ethanol, propan-1-ol, propan-2-ol, butan-1-ol, pentan-1-ol, and 3-methylbutan-1-ol at T = (298.15, 303.15, and 308.15) K
n0 1.40796 298.15 Experimental Determination and Modeling of Densities and Refractive Indices of the Binary Systems Alcohol + Dicyclohexylamine at T = (288.15 to 323.15) K
n0 1.40880 298.15 Excess Molar Enthalpies of Benzyl Alcohol + Alkanols (C1-C6) and Their Correlations at 298.15 K and Ambient Pressure
n0 1.40780 298.15 Effect of Pressure on the Static Relative Permittivities of Alkan-1-ols at 298.15 K
n0 1.40797 298.15 Experimental Liquid-Liquid Equilibria of 1-Alkyl-3-methylimidazolium Hexafluorophosphate with 1-Alcohols
n0 1.40800 298.15 NCMS SOLV-DB
n0 1.40970 298.15 Investigation on vapor liquid equilibrium for 2-propanol + 1-butanol + 1-pentanol at 101.3 kPa
n0 1.40850 298.15 Comparative study of physico-chemical properties of binary mixtures of N,N-dimethylformamide with 1-alkanols at different temperatures
n0 1.40840 298.15 DIELECTRIC AND REFRACTIVE INDEX MEASUREMENTS FOR THE SYSTEMS 1-PENTANOL + OCTANE, OR + DIBUTYL ETHER OR FOR DIBUTYL ETHER + OCTANE AT DIFFERENT TEMPERATURES
n0 1.40890 298.15 Excess Molar Enthalpies of 1,2-Propanediol + Alkan-1-ols (C1-C6) and Their Correlations at 298.15 K and Ambient Pressure (81.5 kPa)
n0 1.40770 298.15 Liquid-Liquid Equilibrium Diagrams of Ethanol + Water + (Ethyl Acetate or 1-Pentanol) at Several Temperatures
n0 1.40703 298.15 Liquid Liquid Phase Equilibria of 1-Propanol + Water + n-Alcohol Ternary Systems at 298.15 K and Atmospheric Pressure
n0 1.40941 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 1.40780 298.15 Excess molar volumes and partial molar volumes for (propionitrile + an alkanol) at T = 298.15 K and p = 0.1 MPa
n0 1.40850 298.15 Bubble temperature measurements on seven binary mixtures formed by ethylbenzene at 94.7 kPa
n0 1.40770 298.15 Density, Refractive Index, and Speed of Sound at 298.15 K and Vapor-Liquid Equilibria at 101.3 kPa for Binary Mixtures of Ethyl Acetate + 1-Pentanol and Ethanol + 2-Methyl-1-propanol
n0 1.40800 298.15 Density, Surface Tension, and Refractive Index of Octane + 1-Alkanol Mixtures at T ) 298.15 K.
n0 1.40764 298.20 Vapor-Liquid Equilibrium Measurements of Ether Alcohol Blends for Investigation on Reformulated Gas
n0 1.40730 298.20 Tie line data for the (water + butyric acid + n-butyl alcohol or amyl alcohol) at T = (298.2, 308.2, and 318.2) K and (water + butyric acid + isoamyl alcohol) at T = 298.2 K
n0 1.40610 303.15 DIELECTRIC AND REFRACTIVE INDEX MEASUREMENTS FOR THE SYSTEMS 1-PENTANOL + 2,5,8,11,14-PENTAOXAPENTADECANE, OR FOR 2,5,8,11,14-PENTAOXAPENTADECANE + OCTANE AT (293.15-303.15) K.
n0 1.40592 303.15 Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrachloroethane and 1-alkanols binary mixtures
n0 1.40650 303.15 DIELECTRIC AND REFRACTIVE INDEX MEASUREMENTS FOR THE SYSTEMS 1-PENTANOL + OCTANE, OR + DIBUTYL ETHER OR FOR DIBUTYL ETHER + OCTANE AT DIFFERENT TEMPERATURES
n0 1.40500 303.15 Thermodynamic properties of (tetradecane + benzene, + toluene, + chlorobenzene, + bromobenzene, + anisole) binary mixtures at T = (298.15, 303.15, and 308.15) K
n0 1.40592 303.15 Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrabromoethane and 1-alkanols binary mixtures
n0 1.40595 303.15 Experimental Determination and Modeling of Densities and Refractive Indices of the Binary Systems Alcohol + Dicyclohexylamine at T = (288.15 to 323.15) K
n0 1.40500 303.15 Thermodynamic interactions in binary mixtures of anisole with ethanol, propan-1-ol, propan-2-ol, butan-1-ol, pentan-1-ol, and 3-methylbutan-1-ol at T = (298.15, 303.15, and 308.15) K
n0 1.40690 303.15 Comparative study of physico-chemical properties of binary mixtures of N,N-dimethylformamide with 1-alkanols at different temperatures
n0 1.40320 308.15 Thermodynamic interactions in binary mixtures of anisole with ethanol, propan-1-ol, propan-2-ol, butan-1-ol, pentan-1-ol, and 3-methylbutan-1-ol at T = (298.15, 303.15, and 308.15) K
n0 1.40388 308.15 Experimental Determination and Modeling of Densities and Refractive Indices of the Binary Systems Alcohol + Dicyclohexylamine at T = (288.15 to 323.15) K
n0 1.40590 308.15 Comparative study of physico-chemical properties of binary mixtures of N,N-dimethylformamide with 1-alkanols at different temperatures
n0 1.40310 308.15 Densities, Viscosities, and Refractive Indices of Binary Mixtures of Methyl Ethyl Ketone + Pentanol Isomers at Different Temperatures
n0 1.40320 308.15 Thermodynamic properties of (tetradecane + benzene, + toluene, + chlorobenzene, + bromobenzene, + anisole) binary mixtures at T = (298.15, 303.15, and 308.15) K
n0 1.40189 313.15 Experimental Determination and Modeling of Densities and Refractive Indices of the Binary Systems Alcohol + Dicyclohexylamine at T = (288.15 to 323.15) K
n0 1.40390 313.15 Comparative study of physico-chemical properties of binary mixtures of N,N-dimethylformamide with 1-alkanols at different temperatures
n0 1.40178 313.15 Thermophysical properties of the binary mixtures (1,8-cineole + 1-alkanol) at T = (298.15 and 313.15) K and at atmospheric pressure
n0 1.39987 318.15 Experimental Determination and Modeling of Densities and Refractive Indices of the Binary Systems Alcohol + Dicyclohexylamine at T = (288.15 to 323.15) K
n0 1.40030 318.15 Mixing thermodynamic properties of 1-butyl-4-methylpyridinium tetrafluoroborate [b4mpy][BF4] with water and with an alkan-1ol (methanol to pentanol)
n0 1.39960 318.15 Densities, Viscosities, and Refractive Indices of Binary Mixtures of Methyl Ethyl Ketone + Pentanol Isomers at Different Temperatures
n0 1.39776 323.15 Experimental Determination and Modeling of Densities and Refractive Indices of the Binary Systems Alcohol + Dicyclohexylamine at T = (288.15 to 323.15) K
ρl [759.77; 822.42] kg/m3 [283.15; 363.15] Show Hide
ρl 821.81 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 821.95 kg/m3 283.15 Densities and Viscosities of Three Binary Monoglyme + 1-Alcohol Systems from (283.15 to 313.15) K
ρl 821.79 kg/m3 283.15 Excess molar enthalpies of R-fenchone + butan-1-ol or + pentan-1-ol. Modeling with COSMO-RS and UNIFAC
ρl 822.42 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 821.90 kg/m3 283.15 Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl 818.34 kg/m3 288.15 Thermodynamic properties of mixtures containing alkoxypropanol and n-alkanol
ρl 818.80 kg/m3 288.15 Excess Molar Volumes of 1,3-Diethyl Propanedioate with Methanol, Ethanol, Propan-1-ol, Propan-2-ol, Butan-2-ol, 2-Methyl-propan-1-ol, and Pentan-1-ol at T = (288.15, 298.15, 313.15, and 328.15) K
ρl 818.59 kg/m3 288.15 Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
ρl 818.79 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 818.56 kg/m3 288.15 Densities and Viscosities for Binary Liquid Mixtures of Pentanol Isomers from (288.15 to 328.15) K at 0.1 MPa
ρl 819.15 kg/m3 288.15 Excess molar enthalpies of diethyl malonate+ (1-butanol, 2-methyl-1-propanol, 1-pentanol, n-heptane, and ethyl acetate) at T= (288.2, 298.2, 313.2, 328.2, 338.2, and 348.2 K) and p = 101.3 kPa
ρl 818.28 kg/m3 288.15 Influence of chain length and degree of branching of alcohol + chlorobenzene mixtures on determination and modelling of VE by CEOS and CEOS/GE mixing rules
ρl 818.30 kg/m3 288.15 Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl 818.30 kg/m3 288.15 Temperature dependence of the volumetric properties of some alkoxypropanols + n-alkanol mixtures
ρl 814.60 kg/m3 293.00 Fluid-Phase Behavior of {1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide, [C6mim][NTf2], + C2-C8 n-Alcohol} Mixtures: Liquid-Liquid Equilibrium and Excess Volumes
ρl 815.00 kg/m3 293.00 KDB
ρl 814.80 kg/m3 293.15 Excess molar volumes of Diisopropylamine + (C1-C5) Alkan-1-ols: application of the ERAS model and cubic EOS
ρl 814.63 kg/m3 293.15 Influence of chain length and degree of branching of alcohol + chlorobenzene mixtures on determination and modelling of VE by CEOS and CEOS/GE mixing rules
ρl 814.81 kg/m3 293.15 Thermodynamic and spectroscopic properties of binary mixtures of n-butylammonium butanoate ionic liquid with alcohols at T = (293.15-313.15) K
ρl 814.59 kg/m3 293.15 Volumetric and Transport Properties of Binary Mixtures of n-Octane + Ethanol, + 1-Propanol, + 1-Butanol, and + 1-Pentanol from (293.15 to 323.15) K at Atmospheric Pressure
ρl 814.50 kg/m3 293.15 Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl 814.68 kg/m3 293.15 Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl 814.60 kg/m3 293.15 Densities and Viscosities of Three Binary Monoglyme + 1-Alcohol Systems from (283.15 to 313.15) K
ρl 814.92 kg/m3 293.15 Densities and Viscosities for Binary Liquid Mixtures of Pentanol Isomers from (288.15 to 328.15) K at 0.1 MPa
ρl 814.53 kg/m3 293.15 Osmotic and apparent molar properties of binary mixtures alcohol + 1-butyl-3-methylimidazolium trifluoromethanesulfonate ionic liquid
ρl 814.89 kg/m3 293.15 Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
ρl 815.13 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 811.00 kg/m3 298.00 Comparative study of physical properties of binary mixtures of halogen free ionic liquids with alcohols
ρl 810.90 kg/m3 298.00 Fluid-Phase Behavior of {1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide, [C6mim][NTf2], + C2-C8 n-Alcohol} Mixtures: Liquid-Liquid Equilibrium and Excess Volumes
ρl 811.10 kg/m3 298.15 Dielectric study of H-bonded interactions in amyl alcohols with ketones and DMSO at T = 298.15 K
ρl 810.83 kg/m3 298.15 Densities and Excess Molar Volumes of N-Methylmorpholine + 1-Alkanol Systems at 298.15 K
ρl 811.10 kg/m3 298.15 Temperature dependence of the volumetric properties of some alkoxypropanols + n-alkanol mixtures
ρl 810.88 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 811.04 kg/m3 298.15 Vapor-liquid equilibria of binary systems composed of polyoxyethylene 4-octylphenyl ether and alcohols: Experimental measurements and correlation
ρl 811.00 kg/m3 298.15 Volumetric, acoustic, and viscometric studies of molecular interactions in binary mixtures of dipropylene glycol dimethyl ether with 1-alkanols at 298.15 K
ρl 811.45 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 810.93 kg/m3 298.15 Densities and Viscosities of Three Binary Monoglyme + 1-Alcohol Systems from (283.15 to 313.15) K
ρl 811.23 kg/m3 298.15 Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
ρl 810.82 kg/m3 298.15 FT-IR studies on excess thermodynamic properties of binary liquid mixtures o-chlorotoluene with 1-propanol, 1-butanol, 1-pentanol, 1-hexanol and 1-heptanol at different temperatures
ρl 811.03 kg/m3 298.15 Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl 810.84 kg/m3 298.15 Study of the Effects of Temperature and Pressure on the Thermodynamic and Acoustic Properties of Pentan-1-ol, 2-Methyl-2-butanol, and Cyclopentanol in the Pressure Range from (0.1 to 100) MPa and Temperature from (293 to 318) K
ρl 811.04 kg/m3 298.15 Densities and Excess Molar Volumes of Cyclopentane (1) + 1-Alkanol (2) Systems at (298.15 and 308.15) K
ρl 811.80 kg/m3 298.15 Excess molar enthalpies of diethyl malonate+ (1-butanol, 2-methyl-1-propanol, 1-pentanol, n-heptane, and ethyl acetate) at T= (288.2, 298.2, 313.2, 328.2, 338.2, and 348.2 K) and p = 101.3 kPa
ρl 810.89 kg/m3 298.15 Excess molar enthalpies of the binary systems: (Dibutyl ether + isomers of pentanol) at T = (298.15 and 308.15) K
ρl 810.88 kg/m3 298.15 Density and Relative Permittivity for 1-Alkanols + Dodecane at 298.15 K
ρl 811.10 kg/m3 298.15 Study of intermolecular interactions through dielectric properties of the mixtures consisting of 1,4-butanediol, primary amyl alcohols and 1,4-dioxane at various temperatures
ρl 811.10 kg/m3 298.15 The study of molecular interactions in 1-ethyl-3-methylimidazolium trifluoromethanesulfonate + 1-pentanol from density, speed of sound and refractive index measurements
ρl 810.90 kg/m3 298.15 Dynamic Viscosities of Diethyl Carbonate with Linear and Secondary Alcohols at Several Temperatures
ρl 811.10 kg/m3 298.15 Surface Properties of Binary Mixtures of Ethylene Glycol with a Series of Aliphatic Alcohols (1-Pentanol, 1-Hexanol, and 1-Heptanol)
ρl 811.26 kg/m3 298.15 Densities and Viscosities for Binary Liquid Mixtures of Pentanol Isomers from (288.15 to 328.15) K at 0.1 MPa
ρl 811.00 kg/m3 298.15 Thermodynamic properties of mixtures containing alkoxypropanol and n-alkanol
ρl 811.14 kg/m3 298.15 Thermodynamic and spectroscopic properties of binary mixtures of n-butylammonium butanoate ionic liquid with alcohols at T = (293.15-313.15) K
ρl 811.40 kg/m3 298.15 Thermodynamics of 1,3-dimethylurea in eight alcohols
ρl 810.93 kg/m3 298.15 Volumetric and Transport Properties of Binary Mixtures of n-Octane + Ethanol, + 1-Propanol, + 1-Butanol, and + 1-Pentanol from (293.15 to 323.15) K at Atmospheric Pressure
ρl 810.82 kg/m3 298.15 Excess molar volumes of Diisopropylamine + (C1-C5) Alkan-1-ols: application of the ERAS model and cubic EOS
ρl 811.47 kg/m3 298.15 Excess Molar Volumes of 1,3-Diethyl Propanedioate with Methanol, Ethanol, Propan-1-ol, Propan-2-ol, Butan-2-ol, 2-Methyl-propan-1-ol, and Pentan-1-ol at T = (288.15, 298.15, 313.15, and 328.15) K
ρl 810.88 kg/m3 298.15 Excess molar enthalpies of methyl isobutyl ketone (MIBK) with alkan-1-ols (C1-C6) and their correlations at 298.15 K
ρl 810.90 kg/m3 298.15 Excess volumes and partial molar volumes of binary liquid mixtures of furfural or 2-methylfuran with alcohols at 298.15 K
ρl 810.12 kg/m3 298.15 Isobaric Vapor Liquid Equilibria of Binary Systems (Propyl Acetate + n-Pentanol), (Propyl Acetate + 1-Methyl-1-butanol), and (Propyl Acetate + 3-Methyl-1-butanol) at 101.3 kPa
ρl 810.88 kg/m3 298.15 Physical Properties of the Pure Deep Eutectic Solvent, [ChCl]:[Lev] (1:2) DES, and Its Binary Mixtures with Alcohols
ρl 810.97 kg/m3 298.15 Influence of chain length and degree of branching of alcohol + chlorobenzene mixtures on determination and modelling of VE by CEOS and CEOS/GE mixing rules
ρl 810.90 kg/m3 298.15 Excess molar enthalpies of R-fenchone + butan-1-ol or + pentan-1-ol. Modeling with COSMO-RS and UNIFAC
ρl 810.80 kg/m3 298.15 Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl 811.29 kg/m3 298.20 Liquid-liquid equilibrium data for ternary systems of water + lactic acid + C4-C7 alcohols at 298.2 K and atmospheric pressure
ρl 807.30 kg/m3 303.00 Fluid-Phase Behavior of {1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide, [C6mim][NTf2], + C2-C8 n-Alcohol} Mixtures: Liquid-Liquid Equilibrium and Excess Volumes
ρl 807.00 kg/m3 303.00 Comparative study of physical properties of binary mixtures of halogen free ionic liquids with alcohols
ρl 807.46 kg/m3 303.15 Thermodynamic and spectroscopic properties of binary mixtures of n-butylammonium butanoate ionic liquid with alcohols at T = (293.15-313.15) K
ρl 810.00 kg/m3 303.15 Study of molecular interactions in the mixtures of some primary alcohols with equimolar mixture of 1-propanol and alkylbenzoates at T = 303.15 K
ρl 807.24 kg/m3 303.15 Volumetric and Transport Properties of Binary Mixtures of n-Octane + Ethanol, + 1-Propanol, + 1-Butanol, and + 1-Pentanol from (293.15 to 323.15) K at Atmospheric Pressure
ρl 807.07 kg/m3 303.15 Excess molar volumes of Diisopropylamine + (C1-C5) Alkan-1-ols: application of the ERAS model and cubic EOS
ρl 807.55 kg/m3 303.15 Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
ρl 807.10 kg/m3 303.15 Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl 807.57 kg/m3 303.15 Densities and Viscosities for Binary Liquid Mixtures of Pentanol Isomers from (288.15 to 328.15) K at 0.1 MPa
ρl 807.28 kg/m3 303.15 Influence of chain length and degree of branching of alcohol + chlorobenzene mixtures on determination and modelling of VE by CEOS and CEOS/GE mixing rules
ρl 807.25 kg/m3 303.15 Densities and Viscosities of Three Binary Monoglyme + 1-Alcohol Systems from (283.15 to 313.15) K
ρl 807.10 kg/m3 303.15 FT-IR studies on excess thermodynamic properties of binary liquid mixtures o-chlorotoluene with 1-propanol, 1-butanol, 1-pentanol, 1-hexanol and 1-heptanol at different temperatures
ρl 807.37 kg/m3 303.15 Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl 807.11 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 807.74 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 803.00 kg/m3 308.00 Comparative study of physical properties of binary mixtures of halogen free ionic liquids with alcohols
ρl 803.52 kg/m3 308.15 Osmotic and apparent molar properties of binary mixtures alcohol + 1-butyl-3-methylimidazolium trifluoromethanesulfonate ionic liquid
ρl 803.30 kg/m3 308.15 Thermodynamic properties of mixtures containing alkoxypropanol and n-alkanol
ρl 804.01 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 803.86 kg/m3 308.15 Densities and Viscosities for Binary Liquid Mixtures of Pentanol Isomers from (288.15 to 328.15) K at 0.1 MPa
ρl 803.68 kg/m3 308.15 Densities and Excess Molar Volumes of Cyclopentane (1) + 1-Alkanol (2) Systems at (298.15 and 308.15) K
ρl 803.30 kg/m3 308.15 Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl 803.53 kg/m3 308.15 Volumetric and Transport Properties of Binary Mixtures of n-Octane + Ethanol, + 1-Propanol, + 1-Butanol, and + 1-Pentanol from (293.15 to 323.15) K at Atmospheric Pressure
ρl 803.56 kg/m3 308.15 Influence of chain length and degree of branching of alcohol + chlorobenzene mixtures on determination and modelling of VE by CEOS and CEOS/GE mixing rules
ρl 803.74 kg/m3 308.15 Thermodynamic and spectroscopic properties of binary mixtures of n-butylammonium butanoate ionic liquid with alcohols at T = (293.15-313.15) K
ρl 804.10 kg/m3 308.15 Temperature dependence of the volumetric properties of some alkoxypropanols + n-alkanol mixtures
ρl 803.50 kg/m3 308.15 Physical Properties of the Pure Deep Eutectic Solvent, [ChCl]:[Lev] (1:2) DES, and Its Binary Mixtures with Alcohols
ρl 803.83 kg/m3 308.15 Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
ρl 803.70 kg/m3 308.15 The study of molecular interactions in 1-ethyl-3-methylimidazolium trifluoromethanesulfonate + 1-pentanol from density, speed of sound and refractive index measurements
ρl 803.70 kg/m3 308.15 Excess molar enthalpies of the binary systems: (Dibutyl ether + isomers of pentanol) at T = (298.15 and 308.15) K
ρl 803.67 kg/m3 308.15 Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl 803.38 kg/m3 308.15 FT-IR studies on excess thermodynamic properties of binary liquid mixtures o-chlorotoluene with 1-propanol, 1-butanol, 1-pentanol, 1-hexanol and 1-heptanol at different temperatures
ρl 800.00 kg/m3 313.00 Comparative study of physical properties of binary mixtures of halogen free ionic liquids with alcohols
ρl 799.82 kg/m3 313.15 Influence of chain length and degree of branching of alcohol + chlorobenzene mixtures on determination and modelling of VE by CEOS and CEOS/GE mixing rules
ρl 800.26 kg/m3 313.15 Excess Molar Volumes of 1,3-Diethyl Propanedioate with Methanol, Ethanol, Propan-1-ol, Propan-2-ol, Butan-2-ol, 2-Methyl-propan-1-ol, and Pentan-1-ol at T = (288.15, 298.15, 313.15, and 328.15) K
ρl 800.08 kg/m3 313.15 Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
ρl 799.71 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 799.40 kg/m3 313.15 Excess molar volumes of Diisopropylamine + (C1-C5) Alkan-1-ols: application of the ERAS model and cubic EOS
ρl 799.94 kg/m3 313.15 Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl 800.57 kg/m3 313.15 Excess molar enthalpies of diethyl malonate+ (1-butanol, 2-methyl-1-propanol, 1-pentanol, n-heptane, and ethyl acetate) at T= (288.2, 298.2, 313.2, 328.2, 338.2, and 348.2 K) and p = 101.3 kPa
ρl 799.80 kg/m3 313.15 Excess molar enthalpies of R-fenchone + butan-1-ol or + pentan-1-ol. Modeling with COSMO-RS and UNIFAC
ρl 799.90 kg/m3 313.15 Densities and Viscosities of Three Binary Monoglyme + 1-Alcohol Systems from (283.15 to 313.15) K
ρl 799.79 kg/m3 313.15 Volumetric and Transport Properties of Binary Mixtures of n-Octane + Ethanol, + 1-Propanol, + 1-Butanol, and + 1-Pentanol from (293.15 to 323.15) K at Atmospheric Pressure
ρl 799.60 kg/m3 313.15 Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl 800.11 kg/m3 313.15 Densities and Viscosities for Binary Liquid Mixtures of Pentanol Isomers from (288.15 to 328.15) K at 0.1 MPa
ρl 800.24 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 799.99 kg/m3 313.15 Thermodynamic and spectroscopic properties of binary mixtures of n-butylammonium butanoate ionic liquid with alcohols at T = (293.15-313.15) K
ρl 796.10 kg/m3 318.15 The study of molecular interactions in 1-ethyl-3-methylimidazolium trifluoromethanesulfonate + 1-pentanol from density, speed of sound and refractive index measurements
ρl 796.29 kg/m3 318.15 Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
ρl 796.03 kg/m3 318.15 Volumetric and Transport Properties of Binary Mixtures of n-Octane + Ethanol, + 1-Propanol, + 1-Butanol, and + 1-Pentanol from (293.15 to 323.15) K at Atmospheric Pressure
ρl 796.43 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 795.80 kg/m3 318.15 Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl 796.32 kg/m3 318.15 Densities and Viscosities for Binary Liquid Mixtures of Pentanol Isomers from (288.15 to 328.15) K at 0.1 MPa
ρl 795.98 kg/m3 318.15 Physical Properties of the Pure Deep Eutectic Solvent, [ChCl]:[Lev] (1:2) DES, and Its Binary Mixtures with Alcohols
ρl 796.17 kg/m3 318.15 Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl 792.36 kg/m3 323.15 Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl 792.48 kg/m3 323.15 Densities and Viscosities for Binary Liquid Mixtures of Pentanol Isomers from (288.15 to 328.15) K at 0.1 MPa
ρl 792.14 kg/m3 323.15 Osmotic coefficients and apparent molar volumes of 1-hexyl-3-methylimidazolium trifluoromethanesulfonate ionic liquid in alcohols
ρl 792.23 kg/m3 323.15 Volumetric and Transport Properties of Binary Mixtures of n-Octane + Ethanol, + 1-Propanol, + 1-Butanol, and + 1-Pentanol from (293.15 to 323.15) K at Atmospheric Pressure
ρl 792.15 kg/m3 323.15 Osmotic and apparent molar properties of binary mixtures alcohol + 1-butyl-3-methylimidazolium trifluoromethanesulfonate ionic liquid
ρl 792.00 kg/m3 323.15 Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl 792.46 kg/m3 323.15 Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
ρl 792.57 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 789.01 kg/m3 328.15 Excess molar enthalpies of diethyl malonate+ (1-butanol, 2-methyl-1-propanol, 1-pentanol, n-heptane, and ethyl acetate) at T= (288.2, 298.2, 313.2, 328.2, 338.2, and 348.2 K) and p = 101.3 kPa
ρl 788.56 kg/m3 328.15 Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
ρl 788.67 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 788.50 kg/m3 328.15 Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl 788.61 kg/m3 328.15 Densities and Viscosities for Binary Liquid Mixtures of Pentanol Isomers from (288.15 to 328.15) K at 0.1 MPa
ρl 788.74 kg/m3 328.15 Excess Molar Volumes of 1,3-Diethyl Propanedioate with Methanol, Ethanol, Propan-1-ol, Propan-2-ol, Butan-2-ol, 2-Methyl-propan-1-ol, and Pentan-1-ol at T = (288.15, 298.15, 313.15, and 328.15) K
ρl 788.82 kg/m3 328.15 Excess molar enthalpies of R-fenchone + butan-1-ol or + pentan-1-ol. Modeling with COSMO-RS and UNIFAC
ρl 788.40 kg/m3 328.15 The study of molecular interactions in 1-ethyl-3-methylimidazolium trifluoromethanesulfonate + 1-pentanol from density, speed of sound and refractive index measurements
ρl 784.59 kg/m3 333.15 Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl 784.66 kg/m3 333.15 Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
ρl 784.72 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 780.62 kg/m3 338.15 Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl 780.70 kg/m3 338.15 Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Pentanol, 2-Pentanol, or 2-Methyl-1-Butanol from (288.15 to 338.15) K at 0.1 MPa
ρl 781.05 kg/m3 338.15 Excess molar enthalpies of diethyl malonate+ (1-butanol, 2-methyl-1-propanol, 1-pentanol, n-heptane, and ethyl acetate) at T= (288.2, 298.2, 313.2, 328.2, 338.2, and 348.2 K) and p = 101.3 kPa
ρl 776.58 kg/m3 343.15 Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl 772.87 kg/m3 348.15 Excess molar enthalpies of diethyl malonate+ (1-butanol, 2-methyl-1-propanol, 1-pentanol, n-heptane, and ethyl acetate) at T= (288.2, 298.2, 313.2, 328.2, 338.2, and 348.2 K) and p = 101.3 kPa
ρl 772.49 kg/m3 348.15 Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl 768.33 kg/m3 353.15 Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl 764.08 kg/m3 358.15 Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl 759.77 kg/m3 363.15 Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
D*i [0.00; 0.00] m2/s [253.13; 364.73] Show Hide
D*i 0.00 m2/s 253.13 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 253.19 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 258.42 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 258.47 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 263.25 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 263.28 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 268.65 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 268.66 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 278.40 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 278.43 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 288.31 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 288.33 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 298.16 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 298.17 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 298.19 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 298.21 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 298.21 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 298.27 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 298.27 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 308.09 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 308.11 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 318.08 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 318.09 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 323.10 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 323.10 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 323.15 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 323.15 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 327.86 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 327.86 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 337.71 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 337.74 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 347.21 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 347.25 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 352.35 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 352.36 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 352.55 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 364.52 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 364.59 Viscous Calibration Liquids for Self-diffusion Measurements
D*i 0.00 m2/s 364.73 Viscous Calibration Liquids for Self-diffusion Measurements
ΔfusS [50.61; 53.70] J/mol×K [194.20; 195.56] Show Hide
ΔfusS 50.61 J/mol×K 194.20 NIST
ΔfusS 50.61 J/mol×K 194.20 NIST
ΔfusS 53.70 J/mol×K 195.56 NIST
ΔfusS 53.70 J/mol×K 195.56 NIST
csound,fluid [1192.80; 1325.90] m/s [283.15; 323.15] Show Hide
csound,fluid 1325.90 m/s 283.15 Excess Molar Enthalpy, Density, and Speed of Sound for the Mixtures a-Pinene + 1- or 2-Pentanol at (283.15, 298.15, and 313.15) K
csound,fluid 1312.50 m/s 288.15 Densities, excess molar volumes, speeds of sound and isothermal compressibilities for {2-(2-hexyloxyethoxy)ethanol + n-alkanol} systems at temperatures between (288.15 and 308.15) K
csound,fluid 1292.50 m/s 293.15 Acoustic, volumetric and osmotic properties of binary mixtures containing the ionic liquid 1-butyl-3-methylimidazolim dicyanamide mixed with primary and secondary alcohols
csound,fluid 1292.52 m/s 293.15 Densities, Excess Molar Volumes, Speeds of Sound at (293.15, 298.15, and 303.15) K and Isentropic Compressibilities at 298.15 K for 1-Butanol, 1-Pentanol, or 1-Hexanol + Dibutylether Systems
csound,fluid 1293.45 m/s 293.15 Densities, excess molar volumes, speeds of sound and isothermal compressibilities for {2-(2-hexyloxyethoxy)ethanol + n-alkanol} systems at temperatures between (288.15 and 308.15) K
csound,fluid 1276.01 m/s 298.15 Densities, excess molar volumes, speeds of sound and isothermal compressibilities for {2-(2-hexyloxyethoxy)ethanol + n-alkanol} systems at temperatures between (288.15 and 308.15) K
csound,fluid 1281.20 m/s 298.15 Ultrasonic speeds and isentropic compressibilities of {difurylmethane + (C1 C6) n-alkanol} binary mixtures at T = 298.15 K
csound,fluid 1274.32 m/s 298.15 Densities, Speeds of Sound, and Isentropic Compressibilities for Binary Mixtures of 2-Ethyl-1-hexanol with 1-Pentanol, 1-Heptanol, or 1-Nonanol at the Temperature 298.15 K
csound,fluid 1274.10 m/s 298.15 Excess Molar Enthalpy, Density, and Speed of Sound for the Mixtures a-Pinene + 1- or 2-Pentanol at (283.15, 298.15, and 313.15) K
csound,fluid 1275.08 m/s 298.15 Densities, Excess Molar Volumes, Speeds of Sound at (293.15, 298.15, and 303.15) K and Isentropic Compressibilities at 298.15 K for 1-Butanol, 1-Pentanol, or 1-Hexanol + Dibutylether Systems
csound,fluid 1274.00 m/s 298.15 Densities, Speeds of Sound, Excess Molar Volumes, and Excess Isentropic Compressibilities at T = (298.15 and 308.15) K for Methyl Methacrylate + 1-Alkanols (1-Butanol, 1-Pentanol, and 1-Heptanol) + Cyclohexane, + Benzene, + Toluene, + p-Xylene, and + Ethylbenzene
csound,fluid 1258.25 m/s 303.15 Densities, excess molar volumes, speeds of sound and isothermal compressibilities for {2-(2-hexyloxyethoxy)ethanol + n-alkanol} systems at temperatures between (288.15 and 308.15) K
csound,fluid 1258.46 m/s 303.15 Densities, Excess Molar Volumes, Speeds of Sound at (293.15, 298.15, and 303.15) K and Isentropic Compressibilities at 298.15 K for 1-Butanol, 1-Pentanol, or 1-Hexanol + Dibutylether Systems
csound,fluid 1243.67 m/s 308.15 Densities, excess molar volumes, speeds of sound and isothermal compressibilities for {2-(2-hexyloxyethoxy)ethanol + n-alkanol} systems at temperatures between (288.15 and 308.15) K
csound,fluid 1240.00 m/s 308.15 Densities, Speeds of Sound, Excess Molar Volumes, and Excess Isentropic Compressibilities at T = (298.15 and 308.15) K for Methyl Methacrylate + 1-Alkanols (1-Butanol, 1-Pentanol, and 1-Heptanol) + Cyclohexane, + Benzene, + Toluene, + p-Xylene, and + Ethylbenzene
csound,fluid 1242.40 m/s 308.15 Acoustic, volumetric and osmotic properties of binary mixtures containing the ionic liquid 1-butyl-3-methylimidazolim dicyanamide mixed with primary and secondary alcohols
csound,fluid 1225.50 m/s 313.15 Excess Molar Enthalpy, Density, and Speed of Sound for the Mixtures a-Pinene + 1- or 2-Pentanol at (283.15, 298.15, and 313.15) K
csound,fluid 1192.80 m/s 323.15 Acoustic, volumetric and osmotic properties of binary mixtures containing the ionic liquid 1-butyl-3-methylimidazolim dicyanamide mixed with primary and secondary alcohols
γ [0.02; 0.03] N/m [293.15; 323.15] Show Hide
γ 0.03 N/m 293.15 The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ 0.03 N/m 293.15 Density and Surface Tension of Binary Mixtures of Acetonitrile + 1-Alkanol at 293.15 K
γ 0.03 N/m 293.15 Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol
γ 0.03 N/m 293.20 KDB
γ 0.02 N/m 298.15 The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ 0.03 N/m 298.15 Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol
γ 0.03 N/m 298.15 Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ 0.03 N/m 298.15 NCMS SOLV-DB
γ 0.02 N/m 303.15 The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ 0.02 N/m 303.15 Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol
γ 0.02 N/m 303.15 Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ 0.02 N/m 308.15 Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ 0.02 N/m 308.15 The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ 0.02 N/m 308.15 Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol
γ 0.02 N/m 313.15 Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ 0.02 N/m 313.15 The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ 0.02 N/m 313.15 Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol
γ 0.02 N/m 318.15 The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ 0.02 N/m 318.15 Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol
γ 0.02 N/m 318.15 Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ 0.02 N/m 323.15 Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol
γ 0.02 N/m 323.15 Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K

Pressure Dependent Properties

Property Value Unit Pressure (kPa) Source
Tboilr 323.20 K 1.70 NIST

Datasets

  1. Isobaric coefficient of expansion, 1/K (1)
  2. Mass density, kg/m3 (8)

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 0.0009
278.15 10000.00 0.0008
278.15 15000.00 0.0008
278.15 20000.00 0.0008
278.15 25000.00 0.0008
278.15 30000.00 0.0008
278.15 35000.00 0.0008
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 0.0009
288.15 10000.00 0.0008
288.15 15000.00 0.0008
288.15 20000.00 0.0008
288.15 25000.00 0.0008
288.15 30000.00 0.0008
288.15 35000.00 0.0008
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 0.0009
298.15 10000.00 0.0009
298.15 15000.00 0.0008
298.15 20000.00 0.0008
298.15 25000.00 0.0008
298.15 30000.00 0.0008
298.15 35000.00 0.0008
298.15 40000.00 0.0008
298.15 45000.00 0.0007
298.15 50000.00 0.0007
298.15 55000.00 0.0007
308.15 5000.00 0.0009
308.15 10000.00 0.0009
308.15 15000.00 0.0009
308.15 20000.00 0.0008
308.15 25000.00 0.0008
308.15 30000.00 0.0008
308.15 35000.00 0.0008
308.15 40000.00 0.0008
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 0.0009
318.15 15000.00 0.0009
318.15 20000.00 0.0009
318.15 25000.00 0.0008
318.15 30000.00 0.0008
318.15 35000.00 0.0008
318.15 40000.00 0.0008
318.15 45000.00 0.0008
318.15 50000.00 0.0007
318.15 55000.00 0.0007
328.15 5000.00 0.0010
328.15 10000.00 0.0009
328.15 15000.00 0.0009
328.15 20000.00 0.0009
328.15 25000.00 0.0008
328.15 30000.00 0.0008
328.15 35000.00 0.0008
328.15 40000.00 0.0008
328.15 45000.00 0.0008
328.15 50000.00 0.0008
328.15 55000.00 0.0007
338.15 5000.00 0.0010
338.15 10000.00 0.0010
338.15 15000.00 0.0009
338.15 20000.00 0.0009
338.15 25000.00 0.0009
338.15 30000.00 0.0008
338.15 35000.00 0.0008
338.15 40000.00 0.0008
338.15 45000.00 0.0008
338.15 50000.00 0.0008
338.15 55000.00 0.0008
348.15 5000.00 0.0010
348.15 10000.00 0.0010
348.15 15000.00 0.0010
348.15 20000.00 0.0009
348.15 25000.00 0.0009
348.15 30000.00 0.0009
348.15 35000.00 0.0008
348.15 40000.00 0.0008
348.15 45000.00 0.0008
348.15 50000.00 0.0008
348.15 55000.00 0.0008
Reference

Mass density, kg/m3

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
293.15 100.00 814.7
293.15 10000.00 821.1
293.15 20000.00 827.3
293.15 30000.00 833.2
293.15 40000.00 838.6
293.15 50000.00 843.6
293.15 60000.00 848.5
293.15 70000.00 853.1
293.15 80000.00 857.4
293.15 90000.00 861.7
293.15 100000.00 865.8
293.15 110000.00 869.6
293.15 120000.00 873.2
293.15 130000.00 876.9
293.15 140000.00 880.3
303.15 100.00 807.3
303.15 10000.00 814.4
303.15 20000.00 820.7
303.15 30000.00 826.7
303.15 40000.00 832.2
303.15 50000.00 837.5
303.15 60000.00 842.4
303.15 70000.00 847.0
303.15 80000.00 851.6
303.15 90000.00 855.8
303.15 100000.00 860.1
303.15 110000.00 864.1
303.15 120000.00 868.0
303.15 130000.00 871.7
303.15 140000.00 875.2
313.15 100.00 799.8
313.15 10000.00 807.4
313.15 20000.00 814.1
313.15 30000.00 820.2
313.15 40000.00 826.0
313.15 50000.00 831.5
313.15 60000.00 836.6
313.15 70000.00 841.4
313.15 80000.00 846.1
313.15 90000.00 850.5
313.15 100000.00 854.8
313.15 110000.00 858.9
313.15 120000.00 862.8
313.15 130000.00 866.6
313.15 140000.00 870.2
323.15 100.00 792.5
323.15 10000.00 800.3
323.15 20000.00 807.3
323.15 30000.00 813.7
323.15 40000.00 819.8
323.15 50000.00 825.4
323.15 60000.00 830.7
323.15 70000.00 835.7
323.15 80000.00 840.4
323.15 90000.00 845.0
323.15 100000.00 849.3
323.15 110000.00 853.6
323.15 120000.00 857.6
323.15 130000.00 861.5
323.15 140000.00 865.3
333.15 100.00 784.4
333.15 10000.00 792.7
333.15 20000.00 800.1
333.15 30000.00 806.8
333.15 40000.00 813.1
333.15 50000.00 818.9
333.15 60000.00 824.4
333.15 70000.00 829.7
333.15 80000.00 834.6
333.15 90000.00 839.2
333.15 100000.00 843.7
333.15 110000.00 848.0
333.15 120000.00 852.1
333.15 130000.00 856.0
333.15 140000.00 860.0
343.15 100.00 776.5
343.15 10000.00 785.2
343.15 20000.00 792.9
343.15 30000.00 799.9
343.15 40000.00 806.6
343.15 50000.00 812.6
343.15 60000.00 818.3
343.15 70000.00 823.7
343.15 80000.00 828.7
343.15 90000.00 833.5
343.15 100000.00 838.2
343.15 110000.00 842.5
343.15 120000.00 846.8
343.15 130000.00 850.9
343.15 140000.00 854.8
353.15 100.00 768.1
353.15 10000.00 777.3
353.15 20000.00 785.6
353.15 30000.00 792.9
353.15 40000.00 799.8
353.15 50000.00 806.1
353.15 60000.00 812.0
353.15 70000.00 817.6
353.15 80000.00 822.8
353.15 90000.00 827.8
353.15 100000.00 832.6
353.15 110000.00 837.2
353.15 120000.00 841.6
353.15 130000.00 845.8
353.15 140000.00 849.7
363.15 100.00 759.4
363.15 10000.00 769.2
363.15 20000.00 777.7
363.15 30000.00 785.6
363.15 40000.00 792.6
363.15 50000.00 799.2
363.15 60000.00 805.5
363.15 70000.00 811.3
363.15 80000.00 816.7
363.15 90000.00 821.8
363.15 100000.00 826.8
363.15 110000.00 831.3
363.15 120000.00 835.8
363.15 130000.00 840.1
363.15 140000.00 844.2
373.15 100.00 750.7
373.15 10000.00 761.2
373.15 20000.00 770.3
373.15 30000.00 778.2
373.15 40000.00 785.7
373.15 50000.00 792.5
373.15 60000.00 798.9
373.15 70000.00 804.9
373.15 80000.00 810.5
373.15 90000.00 815.8
373.15 100000.00 820.9
373.15 110000.00 825.7
373.15 120000.00 830.3
373.15 130000.00 834.7
373.15 140000.00 839.0
383.15 100.00 741.5
383.15 10000.00 752.3
383.15 20000.00 761.9
383.15 30000.00 770.7
383.15 40000.00 778.5
383.15 50000.00 785.7
383.15 60000.00 792.3
383.15 70000.00 798.5
383.15 80000.00 804.3
383.15 90000.00 809.7
383.15 100000.00 815.0
383.15 110000.00 819.9
383.15 120000.00 824.7
383.15 130000.00 829.2
383.15 140000.00 833.5
393.15 100.00 731.7
393.15 10000.00 743.4
393.15 20000.00 753.7
393.15 30000.00 762.8
393.15 40000.00 771.0
393.15 50000.00 778.6
393.15 60000.00 785.6
393.15 70000.00 792.0
393.15 80000.00 798.1
393.15 90000.00 803.7
393.15 100000.00 809.1
393.15 110000.00 814.2
393.15 120000.00 819.1
393.15 130000.00 823.7
393.15 140000.00 828.1
403.15 100.00 721.7
403.15 10000.00 734.4
403.15 20000.00 745.3
403.15 30000.00 754.9
403.15 40000.00 763.4
403.15 50000.00 771.3
403.15 60000.00 778.4
403.15 70000.00 785.1
403.15 80000.00 791.3
403.15 90000.00 797.2
403.15 100000.00 802.8
403.15 110000.00 808.0
403.15 120000.00 813.0
403.15 130000.00 817.8
403.15 140000.00 822.3
Reference
Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
298.15 100.00 810.8
Reference
Fixed Measured
Temperature, K - Fluid (supercritical or subcritical phases) Pressure, kPa - Fluid (supercritical or subcritical phases) Mass density, kg/m3 - Fluid (supercritical or subcritical phases)
312.96 512.00 799.65
312.96 1022.00 800.04
312.96 1998.00 800.77
312.96 3005.00 801.53
312.96 4003.00 802.28
312.96 5002.00 803.02
312.96 6018.00 803.76
312.96 6994.00 804.49
312.96 8008.00 805.21
312.96 9005.00 805.93
312.96 10008.00 806.66
312.96 11008.00 807.37
312.96 12000.00 808.07
312.96 13024.00 808.78
312.96 13987.00 809.45
312.96 15014.00 810.14
312.96 15991.00 810.8
312.96 17019.00 811.48
312.96 17991.00 812.12
312.96 19007.00 812.79
312.96 19992.00 813.44
312.96 21031.00 814.1
312.96 22041.00 814.76
312.96 23014.00 815.41
312.96 24003.00 816.04
312.96 25037.00 816.73
322.89 520.00 792.06
322.89 1010.00 792.47
322.89 2005.00 793.27
322.89 3007.00 794.07
322.89 4005.00 794.86
322.89 5018.00 795.63
322.89 6001.00 796.42
322.89 7016.00 797.2
322.89 8020.00 797.97
322.89 8997.00 798.71
322.89 10001.00 799.47
322.89 11005.00 800.21
322.89 11996.00 800.95
322.89 13002.00 801.68
322.89 14013.00 802.4
322.89 15005.00 803.11
322.89 16014.00 803.82
322.89 17001.00 804.51
322.89 18016.00 805.21
322.89 19012.00 805.89
322.89 19992.00 806.56
322.89 21036.00 807.26
322.89 22003.00 807.92
322.89 23024.00 808.61
322.89 23994.00 809.26
322.89 25023.00 810.0
332.79 493.00 784.29
332.79 1014.00 784.76
332.79 2006.00 785.61
332.79 3025.00 786.48
332.79 4011.00 787.28
332.79 5020.00 788.11
332.79 6003.00 788.91
332.79 6997.00 789.73
332.79 8009.00 790.54
332.79 8995.00 791.31
332.79 9996.00 792.12
332.79 11018.00 792.9
332.79 11995.00 793.66
332.79 13023.00 794.45
332.79 13999.00 795.19
332.79 15010.00 795.95
332.79 16028.00 796.68
332.79 17003.00 797.41
332.79 18040.00 798.14
332.79 19004.00 798.84
332.79 20035.00 799.59
332.79 21024.00 800.29
332.79 21993.00 800.97
332.79 23039.00 801.71
332.79 24015.00 802.4
332.79 25022.00 803.12
342.76 505.00 776.31
342.76 997.00 776.77
342.76 1995.00 777.69
342.76 3011.00 778.59
342.76 4012.00 779.47
342.76 5011.00 780.34
342.76 6011.00 781.22
342.76 7003.00 782.03
342.76 8015.00 782.91
342.76 9000.00 783.73
342.76 10019.00 784.58
342.76 11020.00 785.4
342.76 12002.00 786.2
342.76 13016.00 787.02
342.76 14024.00 787.81
342.76 15002.00 788.59
342.76 16007.00 789.36
342.76 17037.00 790.15
342.76 17988.00 790.87
342.76 19037.00 791.66
342.76 20003.00 792.38
342.76 21015.00 793.14
342.76 22019.00 793.88
342.76 23039.00 794.62
342.76 24027.00 795.36
342.76 25028.00 796.1
352.71 508.00 768.15
352.71 1011.00 768.66
352.71 1995.00 769.61
352.71 3014.00 770.57
352.71 3998.00 771.49
352.71 5022.00 772.45
352.71 6012.00 773.35
352.71 7006.00 774.26
352.71 8024.00 775.17
352.71 9005.00 776.05
352.71 10016.00 776.94
352.71 11026.00 777.81
352.71 12001.00 778.65
352.71 13002.00 779.5
352.71 14026.00 780.35
352.71 15000.00 781.18
352.71 16005.00 781.98
352.71 17023.00 782.81
352.71 18003.00 783.59
352.71 19049.00 784.43
352.71 20035.00 785.2
352.71 21002.00 785.96
352.71 21995.00 786.73
352.71 23020.00 787.52
352.71 24045.00 788.32
352.71 25009.00 789.05
362.59 517.00 759.7
362.59 1023.00 760.25
362.59 2005.00 761.26
362.59 3010.00 762.29
362.59 3998.00 763.28
362.59 5006.00 764.25
362.59 6013.00 765.23
362.59 7014.00 766.21
362.59 8007.00 767.16
362.59 9020.00 768.1
362.59 10006.00 769.02
362.59 10991.00 769.93
362.59 12025.00 770.87
362.59 13008.00 771.76
362.59 13998.00 772.62
362.59 15017.00 773.51
362.59 16000.00 774.37
362.59 17013.00 775.24
362.59 18032.00 776.11
362.59 19003.00 776.9
362.59 20030.00 777.77
362.59 20987.00 778.55
362.59 22033.00 779.4
362.59 23000.00 780.2
362.59 24031.00 781.02
362.59 25026.00 781.82
Reference
Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
278.15 100.00 825.2
278.15 1000.00 825.8
278.15 5000.00 828.5
278.15 10000.00 831.6
278.15 15000.00 834.7
278.15 20000.00 837.6
278.15 25000.00 840.4
278.15 30000.00 843.2
278.15 35000.00 845.9
278.15 40000.00 848.6
278.15 45000.00 851.1
278.15 50000.00 853.6
278.15 55000.00 856.1
278.15 60000.00 858.4
288.15 100.00 818.0
288.15 1000.00 818.7
288.15 5000.00 821.5
288.15 10000.00 824.8
288.15 15000.00 828.0
288.15 20000.00 831.1
288.15 25000.00 834.0
288.15 30000.00 836.9
288.15 35000.00 839.7
288.15 40000.00 842.4
288.15 45000.00 845.0
288.15 50000.00 847.6
288.15 55000.00 850.1
288.15 60000.00 852.5
298.15 100.00 810.7
298.15 1000.00 811.3
298.15 5000.00 814.2
298.15 10000.00 817.7
298.15 15000.00 821.0
298.15 20000.00 824.3
298.15 25000.00 827.3
298.15 30000.00 830.3
298.15 35000.00 833.2
298.15 40000.00 836.0
298.15 45000.00 838.7
298.15 50000.00 841.4
298.15 55000.00 844.0
298.15 60000.00 846.4
308.15 100.00 803.3
308.15 1000.00 804.0
308.15 5000.00 807.0
308.15 10000.00 810.7
308.15 15000.00 814.0
308.15 20000.00 817.5
308.15 25000.00 820.7
308.15 30000.00 823.8
308.15 35000.00 826.8
308.15 40000.00 829.7
308.15 45000.00 832.5
308.15 50000.00 835.3
308.15 55000.00 838.0
308.15 60000.00 840.4
318.15 100.00 795.8
318.15 1000.00 796.6
318.15 5000.00 799.8
318.15 10000.00 803.6
318.15 15000.00 807.2
318.15 20000.00 810.7
318.15 25000.00 814.0
318.15 30000.00 817.3
318.15 35000.00 820.4
318.15 40000.00 823.4
318.15 45000.00 826.3
318.15 50000.00 829.1
318.15 55000.00 831.9
318.15 60000.00 834.6
328.15 100.00 788.2
328.15 1000.00 789.0
328.15 5000.00 792.3
328.15 10000.00 796.3
328.15 15000.00 800.1
328.15 20000.00 803.8
328.15 25000.00 807.2
328.15 30000.00 810.6
328.15 35000.00 813.8
328.15 40000.00 817.0
328.15 45000.00 820.0
328.15 50000.00 822.9
328.15 55000.00 825.8
328.15 60000.00 828.4
338.15 100.00 780.3
338.15 1000.00 781.2
338.15 5000.00 784.8
338.15 10000.00 788.9
338.15 15000.00 792.9
338.15 20000.00 796.7
338.15 25000.00 800.3
338.15 30000.00 803.8
338.15 35000.00 807.2
338.15 40000.00 810.5
338.15 45000.00 813.6
338.15 50000.00 816.6
338.15 55000.00 819.6
338.15 60000.00 822.5
348.15 100.00 772.3
348.15 1000.00 773.1
348.15 5000.00 776.9
348.15 10000.00 781.2
348.15 15000.00 785.5
348.15 20000.00 789.5
348.15 25000.00 793.3
348.15 30000.00 796.9
348.15 35000.00 800.4
348.15 40000.00 803.8
348.15 45000.00 807.1
348.15 50000.00 810.3
348.15 55000.00 813.3
348.15 60000.00 816.2
358.15 100.00 763.8
358.15 1000.00 764.8
358.15 5000.00 768.8
358.15 10000.00 773.5
358.15 15000.00 777.9
358.15 20000.00 782.1
358.15 25000.00 786.1
358.15 30000.00 789.9
358.15 35000.00 793.6
358.15 40000.00 797.1
358.15 45000.00 800.5
358.15 50000.00 803.8
358.15 55000.00 807.0
358.15 60000.00 810.0
Reference
Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
298.15 2003.00 811.93
298.15 3999.00 813.3
298.15 6003.00 814.64
298.15 8005.00 815.96
298.15 10001.00 817.26
298.15 13000.00 819.15
298.15 16004.00 821.0
298.15 19006.00 822.8
298.15 22000.00 824.56
298.15 24998.00 826.27
323.15 1999.00 794.19
323.15 4001.00 795.77
323.15 6001.00 797.32
323.15 8000.00 798.83
323.15 9998.00 800.31
323.15 12999.00 802.47
323.15 16001.00 804.56
323.15 19002.00 806.59
323.15 22001.00 808.56
323.15 25002.00 810.48
Reference
Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
298.15 2000.00 813.0
298.15 4000.00 814.4
298.15 6000.00 815.8
298.15 8010.00 817.1
298.15 10000.00 818.5
298.15 13000.00 820.4
298.15 16000.00 822.3
298.15 19010.00 824.1
298.15 22000.00 825.9
298.15 25000.00 827.6
298.15 27990.00 829.4
298.15 29980.00 830.4
303.16 1980.00 808.8
303.16 3980.00 810.2
303.16 6010.00 811.7
303.16 8020.00 813.0
303.16 10030.00 814.4
303.16 12990.00 816.4
303.16 15980.00 818.4
303.15 19000.00 820.3
303.16 22010.00 822.1
303.16 25000.00 823.9
303.15 27980.00 825.6
303.16 29990.00 826.7
313.15 1990.00 800.6
313.15 4000.00 802.2
313.15 5980.00 803.7
313.15 7980.00 805.1
313.15 10020.00 806.6
313.15 13010.00 808.7
313.16 15980.00 810.8
313.15 19020.00 812.8
313.15 21980.00 814.7
313.16 24990.00 816.6
313.16 28000.00 818.4
313.15 30020.00 819.6
323.15 2000.00 793.5
323.15 4000.00 795.0
323.15 6000.00 796.7
323.15 8000.00 798.2
323.15 10000.00 799.6
323.15 13000.00 801.9
323.15 16000.00 804.0
323.15 19000.00 806.1
323.15 22000.00 808.2
323.15 25000.00 810.2
323.15 27990.00 812.1
323.15 29990.00 813.4
Reference
Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
293.15 100.00 815.25
293.15 5000.00 818.83
293.15 10000.00 822.19
293.15 15000.00 825.37
293.15 20000.00 828.41
293.15 25000.00 831.36
293.15 30000.00 834.24
293.15 35000.00 837.11
303.15 100.00 808.05
303.15 5000.00 811.93
303.15 10000.00 815.5
303.15 15000.00 818.82
303.15 20000.00 821.92
303.15 25000.00 824.88
303.15 30000.00 827.74
303.15 35000.00 830.55
313.15 100.00 800.67
313.15 5000.00 804.61
313.15 10000.00 808.28
313.15 15000.00 811.75
313.15 20000.00 815.06
313.15 25000.00 818.26
313.15 30000.00 821.41
313.15 35000.00 824.56
Reference
Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
298.15 100.00 810.8
Reference

Correlations

Property Value Unit Temperature (K) Source
Cp,gas [98.89; 341.10] J/mol×K [200.00; 1500.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is Cp,gas in J/mol×K, T in K
Coefficient A7.81440e+01
Coefficient B-5.73830e+02
Coefficient C5.87324e+00
Coefficient D1.54310e-04
Coefficient E-6.67450e-08
Temperature range, min.200.00
Temperature range, max.1500.00
Cp,gas 98.89 J/mol×K 200.00 Calculated Property
Cp,gas 148.43 J/mol×K 344.44 Calculated Property
Cp,gas 194.77 J/mol×K 488.89 Calculated Property
Cp,gas 232.33 J/mol×K 633.33 Calculated Property
Cp,gas 262.18 J/mol×K 777.78 Calculated Property
Cp,gas 285.94 J/mol×K 922.22 Calculated Property
Cp,gas 304.91 J/mol×K 1066.67 Calculated Property
Cp,gas 320.02 J/mol×K 1211.11 Calculated Property
Cp,gas 331.92 J/mol×K 1355.56 Calculated Property
Cp,gas 341.10 J/mol×K 1500.00 Calculated Property
Property Value Unit Temperature (K) Source
Cp,liquid [163.68; 288.43] J/mol×K [200.14; 390.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is Cp,liquid in J/mol×K, T in K
Coefficient A1.51460e+02
Coefficient B7.21520e+02
Coefficient C-1.04769e+01
Coefficient D5.96040e-02
Coefficient E-6.37670e-05
Temperature range, min.200.14
Temperature range, max.390.00
Cp,liquid 163.68 J/mol×K 200.14 Calculated Property
Cp,liquid 168.75 J/mol×K 221.24 Calculated Property
Cp,liquid 175.99 J/mol×K 242.33 Calculated Property
Cp,liquid 185.87 J/mol×K 263.43 Calculated Property
Cp,liquid 198.72 J/mol×K 284.52 Calculated Property
Cp,liquid 214.52 J/mol×K 305.62 Calculated Property
Cp,liquid 232.78 J/mol×K 326.71 Calculated Property
Cp,liquid 252.39 J/mol×K 347.81 Calculated Property
Cp,liquid 271.65 J/mol×K 368.90 Calculated Property
Cp,liquid 288.43 J/mol×K 390.00 Calculated Property
Property Value Unit Temperature (K) Source
η [0.0161034; 0.0002081] Pa×s [253.15; 450.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = exp(A + B/T + C·ln(T) + D·T^E)
Y is η in Pa×s, T in K
Coefficient A-2.96960e+01
Coefficient B3.12620e+03
Coefficient C2.41670e+00
Coefficient D-2.43270e-06
Coefficient E2.00000e+00
Temperature range, min.253.15
Temperature range, max.450.00
η 0.0161034 Pa×s 253.15 Calculated Property
η 0.0071641 Pa×s 275.02 Calculated Property
η 0.0036189 Pa×s 296.89 Calculated Property
η 0.0020192 Pa×s 318.77 Calculated Property
η 0.0012193 Pa×s 340.64 Calculated Property
η 0.0007847 Pa×s 362.51 Calculated Property
η 0.0005319 Pa×s 384.38 Calculated Property
η 0.0003762 Pa×s 406.26 Calculated Property
η 0.0002757 Pa×s 428.13 Calculated Property
η 0.0002081 Pa×s 450.00 Calculated Property
Property Value Unit Temperature (K) Source
ΔvapH [70.78; 0.39] kJ/mol [195.56; 588.10] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc
Y is ΔvapH in kJ/mol, T in K
Coefficient A1.18530e+02
Coefficient B1.96680e+00
Coefficient C-2.57410e+00
Coefficient D1.62680e+00
Coefficient E-4.10370e-01
Critical temperature, Tc (K)5.88150e+02
Temperature range, min.195.56
Temperature range, max.588.10
ΔvapH 70.78 kJ/mol 195.56 Calculated Property
ΔvapH 64.64 kJ/mol 239.18 Calculated Property
ΔvapH 59.18 kJ/mol 282.79 Calculated Property
ΔvapH 54.08 kJ/mol 326.41 Calculated Property
ΔvapH 49.07 kJ/mol 370.02 Calculated Property
ΔvapH 43.85 kJ/mol 413.64 Calculated Property
ΔvapH 38.06 kJ/mol 457.25 Calculated Property
ΔvapH 31.11 kJ/mol 500.87 Calculated Property
ΔvapH 21.73 kJ/mol 544.48 Calculated Property
ΔvapH 0.39 kJ/mol 588.10 Calculated Property
Property Value Unit Temperature (K) Source
Pvap [1.33; 202.66] kPa [317.91; 433.96] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.45991e+01
Coefficient B-3.07041e+03
Coefficient C-1.03369e+02
Temperature range, min.317.91
Temperature range, max.433.96
Pvap 1.33 kPa 317.91 Calculated Property
Pvap 3.00 kPa 330.80 Calculated Property
Pvap 6.19 kPa 343.70 Calculated Property
Pvap 11.87 kPa 356.59 Calculated Property
Pvap 21.36 kPa 369.49 Calculated Property
Pvap 36.40 kPa 382.38 Calculated Property
Pvap 59.19 kPa 395.28 Calculated Property
Pvap 92.36 kPa 408.17 Calculated Property
Pvap 139.01 kPa 421.07 Calculated Property
Pvap 202.66 kPa 433.96 Calculated Property
Pvap [4.07e-07; 3839.32] kPa [195.56; 588.10] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = exp(A + B/T + C·ln(T) + D·T^E)
Y is Pvap in kPa, T in K
Coefficient A1.44086e+02
Coefficient B-1.19389e+04
Coefficient C-1.85910e+01
Coefficient D8.73559e-06
Coefficient E2.00000e+00
Temperature range, min.195.56
Temperature range, max.588.10
Pvap 4.07e-07 kPa 195.56 Calculated Property
Pvap 7.78e-04 kPa 239.18 Calculated Property
Pvap 0.09 kPa 282.79 Calculated Property
Pvap 2.30 kPa 326.41 Calculated Property
Pvap 21.70 kPa 370.02 Calculated Property
Pvap 110.65 kPa 413.64 Calculated Property
Pvap 375.25 kPa 457.25 Calculated Property
Pvap 965.37 kPa 500.87 Calculated Property
Pvap 2054.80 kPa 544.48 Calculated Property
Pvap 3839.32 kPa 588.10 Calculated Property
Pvap [3.32e-07; 3863.36] kPa [195.56; 588.00] 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 A1.49346e+02
Coefficient B-1.21964e+04
Coefficient C-1.93819e+01
Coefficient D9.39571e-06
Coefficient E0.00000e+00
Temperature range, min.195.56
Temperature range, max.588.00
Pvap 3.32e-07 kPa 195.56 Calculated Property
Pvap 6.96e-04 kPa 239.16 Calculated Property
Pvap 0.09 kPa 282.77 Calculated Property
Pvap 2.21 kPa 326.37 Calculated Property
Pvap 21.18 kPa 369.98 Calculated Property
Pvap 108.89 kPa 413.58 Calculated Property
Pvap 371.28 kPa 457.19 Calculated Property
Pvap 959.68 kPa 500.79 Calculated Property
Pvap 2053.63 kPa 544.40 Calculated Property
Pvap 3863.36 kPa 588.00 Calculated Property
Pvap [211.77; 1140.16] kPa [437.79; 513.79] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.37553e+01
Coefficient B-2.54691e+03
Coefficient C-1.34578e+02
ReferenceAmbrose, Sprake, et al., 1975
CommentCoefficents calculated by NIST from author's data.
Temperature range, min.437.79
Temperature range, max.513.79
Pvap 211.77 kPa 437.79 Calculated Property
Pvap 265.89 kPa 446.23 Calculated Property
Pvap 329.86 kPa 454.68 Calculated Property
Pvap 404.71 kPa 463.12 Calculated Property
Pvap 491.48 kPa 471.57 Calculated Property
Pvap 591.21 kPa 480.01 Calculated Property
Pvap 704.94 kPa 488.46 Calculated Property
Pvap 833.69 kPa 496.90 Calculated Property
Pvap 978.44 kPa 505.35 Calculated Property
Pvap 1140.16 kPa 513.79 Calculated Property
Pvap [7.15; 177.54] kPa [347.91; 429.13] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.45620e+01
Coefficient B-2.98804e+03
Coefficient C-1.10669e+02
ReferenceAmbrose and Sprake, 1970
CommentCoefficents calculated by NIST from author's data.
Temperature range, min.347.91
Temperature range, max.429.13
Pvap 7.15 kPa 347.91 Calculated Property
Pvap 11.34 kPa 356.93 Calculated Property
Pvap 17.42 kPa 365.96 Calculated Property
Pvap 25.97 kPa 374.98 Calculated Property
Pvap 37.73 kPa 384.01 Calculated Property
Pvap 53.50 kPa 393.03 Calculated Property
Pvap 74.25 kPa 402.06 Calculated Property
Pvap 101.04 kPa 411.08 Calculated Property
Pvap 135.04 kPa 420.11 Calculated Property
Pvap 177.54 kPa 429.13 Calculated Property
Pvap [0.57; 102.21] kPa [307.10; 411.00] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.53876e+01
Coefficient B-3.43672e+03
Coefficient C-9.16210e+01
ReferenceKemme and Kreps, 1969
Temperature range, min.307.10
Temperature range, max.411.00
Pvap 0.57 kPa 307.10 Calculated Property
Pvap 1.28 kPa 318.64 Calculated Property
Pvap 2.67 kPa 330.19 Calculated Property
Pvap 5.19 kPa 341.73 Calculated Property
Pvap 9.52 kPa 353.28 Calculated Property
Pvap 16.58 kPa 364.82 Calculated Property
Pvap 27.61 kPa 376.37 Calculated Property
Pvap 44.19 kPa 387.91 Calculated Property
Pvap 68.27 kPa 399.46 Calculated Property
Pvap 102.21 kPa 411.00 Calculated Property
Property Value Unit Temperature (K) Source
ρl [884.27; 271.16] kg/m3 [195.56; 588.10] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A / B^(1 + (1 − T/C)^D)
Y is ρl in kg/m3, T in K
Coefficient A4.77208e+01
Coefficient B2.18480e-01
Coefficient C5.88150e+02
Coefficient D2.08120e-01
Temperature range, min.195.56
Temperature range, max.588.10
ρl 884.27 kg/m3 195.56 Calculated Property
ρl 854.83 kg/m3 239.18 Calculated Property
ρl 823.46 kg/m3 282.79 Calculated Property
ρl 789.68 kg/m3 326.41 Calculated Property
ρl 752.79 kg/m3 370.02 Calculated Property
ρl 711.69 kg/m3 413.64 Calculated Property
ρl 664.49 kg/m3 457.25 Calculated Property
ρl 607.30 kg/m3 500.87 Calculated Property
ρl 529.41 kg/m3 544.48 Calculated Property
ρl 271.16 kg/m3 588.10 Calculated Property
Property Value Unit Temperature (K) Source
γ [0.03; 0.02] N/m [194.15; 410.65] Jasper (1972), surface tension of pure liquid compounds Compiled value Show Hide
EquationY = A + B·T + C·T² + D·T³ + E·T⁴
Y is γ in N/m, T in K
Coefficient A5.14133e-02
Coefficient B-8.74000e-05
Coefficient C0.00000e+00
Coefficient D0.00000e+00
Coefficient E0.00000e+00
Temperature range, min.194.15
Temperature range, max.410.65
γ 0.03 N/m 194.15 Calculated Property
γ 0.03 N/m 218.21 Calculated Property
γ 0.03 N/m 242.26 Calculated Property
γ 0.03 N/m 266.32 Calculated Property
γ 0.03 N/m 290.37 Calculated Property
γ 0.02 N/m 314.43 Calculated Property
γ 0.02 N/m 338.48 Calculated Property
γ 0.02 N/m 362.54 Calculated Property
γ 0.02 N/m 386.59 Calculated Property
γ 0.02 N/m 410.65 Calculated Property
γ [0.03; 0.01] N/m [273.15; 503.15] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is γ in N/m, T in K
Coefficient A-6.67810e-02
Coefficient B-4.59480e+01
Coefficient C-1.82890e+00
Coefficient D-1.33470e-03
Coefficient E-5.55300e-08
Temperature range, min.273.15
Temperature range, max.503.15
γ 0.03 N/m 273.15 Calculated Property
γ 0.03 N/m 298.71 Calculated Property
γ 0.02 N/m 324.26 Calculated Property
γ 0.02 N/m 349.82 Calculated Property
γ 0.02 N/m 375.37 Calculated Property
γ 0.02 N/m 400.93 Calculated Property
γ 0.01 N/m 426.48 Calculated Property
γ 0.01 N/m 452.04 Calculated Property
γ 0.01 N/m 477.59 Calculated Property
γ 0.01 N/m 503.15 Calculated Property
Property Value Unit Temperature (K) Source
λgas [0.01; 0.11] W/m×K [195.56; 990.95] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A·T^B / (1 + C/T + D/T²)
Y is λgas in W/m×K, T in K
Coefficient A1.22150e+03
Coefficient B9.51170e-01
Coefficient C8.00140e+09
Coefficient D-2.82550e+11
Temperature range, min.195.56
Temperature range, max.990.95
λgas 0.01 W/m×K 195.56 Calculated Property
λgas 0.01 W/m×K 283.94 Calculated Property
λgas 0.02 W/m×K 372.31 Calculated Property
λgas 0.03 W/m×K 460.69 Calculated Property
λgas 0.04 W/m×K 549.07 Calculated Property
λgas 0.05 W/m×K 637.44 Calculated Property
λgas 0.06 W/m×K 725.82 Calculated Property
λgas 0.08 W/m×K 814.20 Calculated Property
λgas 0.09 W/m×K 902.57 Calculated Property
λgas 0.11 W/m×K 990.95 Calculated Property
Property Value Unit Temperature (K) Source
λliquid [0.16; 0.15] W/m×K [273.15; 373.15] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is λliquid in W/m×K, T in K
Coefficient A1.46790e-01
Coefficient B2.01570e+05
Coefficient C-2.09750e+03
Coefficient D7.25500e+00
Coefficient E-8.39730e-03
Temperature range, min.273.15
Temperature range, max.373.15
λliquid 0.16 W/m×K 273.15 Calculated Property
λliquid 0.16 W/m×K 284.26 Calculated Property
λliquid 0.16 W/m×K 295.37 Calculated Property
λliquid 0.15 W/m×K 306.48 Calculated Property
λliquid 0.15 W/m×K 317.59 Calculated Property
λliquid 0.15 W/m×K 328.71 Calculated Property
λliquid 0.15 W/m×K 339.82 Calculated Property
λliquid 0.15 W/m×K 350.93 Calculated Property
λliquid 0.15 W/m×K 362.04 Calculated Property
λliquid 0.15 W/m×K 373.15 Calculated Property

Similar Compounds

hexanol-d3. 1-Hexanol. 1,5-Pentanediol. 1-Heptanol. 1-Tetradecanol. 1-Heptacosanol. 1-Octadecanol. 1-Octanol. 1-Hexadecanol. n-Pentadecanol. n-Nonadecanol-1. n-Tridecan-1-ol. 1-Heneicosanol. 1-Tricosanol. 1-Tetracosanol.

Find more compounds similar to 1-Pentanol.

Mixtures

Find more mixtures with 1-Pentanol.

Sources

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