Chemical Properties of 1-Butanol, 3-methyl- (CAS 123-51-3)

1-Butanol, 3-methyl-

InChI
InChI=1S/C5H12O/c1-5(2)3-4-6/h5-6H,3-4H2,1-2H3
InChI Key
PHTQWCKDNZKARW-UHFFFAOYSA-N
Formula
C5H12O
SMILES
CC(C)CCO
Molecular Weight1
88.15
CAS
123-51-3
Other Names
  • 2-Methyl-4-butanol
  • 3-Methylbutanol
  • 3-Metil-butanolo
  • 3-methyl-1-butanol
  • 3-methylbutan-1-ol
  • 3-methylbutanoI
  • Alcool amilico
  • Alcool isoamylique
  • Amylowy alkohol
  • Butan-1-ol, 3-methyl
  • Butanol, 3-methyl-
  • Fermentation amyl alcohol
  • Fusel Oil
  • Isoamyl alcohol (3-methyl butanol)
  • Isoamyl alcohol, primary
  • Isoamylol
  • Isobutyl carbinol
  • Isopentan-1-ol
  • Methyl-3-butan-1-ol
  • NSC 1029
  • i-Amyl alcohol
  • iso-amylalkohol
  • isoamyl alcohol
  • isopentanol
  • isopentyl alcohol
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Physical Properties

Property Value Unit Source
ω 0.5800 PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ΔcH°liquid [-3326.60; -3326.20] kJ/mol Show Hide
ΔcH°liquid -3326.60 ± 1.60 kJ/mol NIST
ΔcH°liquid -3326.20 ± 0.50 kJ/mol NIST
Cp,liquid 209.30 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 1.80 debye KDB
ΔfG° -148.04 kJ/mol Joback Calculated Property
ΔfH°gas [-302.30; -300.80] kJ/mol Show Hide
ΔfH°gas -302.30 kJ/mol KDB
ΔfH°gas -300.80 kJ/mol NIST
ΔfH°gas -301.30 ± 1.50 kJ/mol NIST
ΔfH°liquid [-356.40; -355.90] kJ/mol Show Hide
ΔfH°liquid -355.90 ± 1.60 kJ/mol NIST
ΔfH°liquid -356.40 ± 0.59 kJ/mol NIST
ΔfusH° 9.27 kJ/mol Joback Calculated Property
ΔvapH° [44.18; 55.63] kJ/mol Show Hide
ΔvapH° 55.63 kJ/mol NIST
ΔvapH° 55.30 kJ/mol NIST
ΔvapH° 55.00 ± 1.30 kJ/mol NIST
ΔvapH° 55.10 kJ/mol NIST
ΔvapH° 54.30 kJ/mol NIST
ΔvapH° Outlier 44.18 ± 0.02 kJ/mol NIST
IE 9.99 eV Relay (1.0) Calculated Property
log10WS [-0.52; -0.51]   Show Hide
log10WS -0.52 Aq. Solubility Prediction
log10WS -0.51 Estimated Solubility
logPoct/wat 1.025 Crippen Calculated Property
McVol 87.180 ml/mol McGowan Calculated Property
NFPA Fire 2 KDB
NFPA Health 1 KDB
Pc [3850.35; 4559.63] kPa Show Hide
Pc 3930.00 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 3930.00 kPa KDB
Pc 3930.00 ± 20.00 kPa NIST
Pc 3930.00 ± 40.00 kPa NIST
Pc Outlier 4559.63 ± 202.65 kPa NIST
Inp [700.00; 773.00]   Show Hide
Inp 723.00 NIST
Inp 733.00 NIST
Inp 721.00 NIST
Inp 723.00 NIST
Inp 727.00 NIST
Inp 738.00 NIST
Inp 733.00 NIST
Inp 721.00 NIST
Inp 723.00 NIST
Inp 727.00 NIST
Inp 738.00 NIST
Inp 733.00 NIST
Inp 721.00 NIST
Inp 720.00 NIST
Inp 718.00 NIST
Inp 725.00 NIST
Inp 725.00 NIST
Inp 719.00 NIST
Inp 719.00 NIST
Inp 712.00 NIST
Inp 726.00 NIST
Inp 730.00 NIST
Inp 727.00 NIST
Inp 741.00 NIST
Inp 725.00 NIST
Inp 725.00 NIST
Inp 744.00 NIST
Inp 747.00 NIST
Inp 734.00 NIST
Inp 732.00 NIST
Inp 727.00 NIST
Inp 706.00 NIST
Inp 718.00 NIST
Inp 738.20 NIST
Inp 756.00 NIST
Inp 734.00 NIST
Inp 740.00 NIST
Inp 736.00 NIST
Inp 736.00 NIST
Inp 736.00 NIST
Inp 730.00 NIST
Inp 754.00 NIST
Inp 719.00 NIST
Inp 708.00 NIST
Inp 731.00 NIST
Inp Outlier 700.00 NIST
Inp 736.00 NIST
Inp 740.00 NIST
Inp 743.00 NIST
Inp 736.00 NIST
Inp Outlier 700.00 NIST
Inp 740.00 NIST
Inp 721.00 NIST
Inp Outlier 700.00 NIST
Inp Outlier 700.00 NIST
Inp 743.00 NIST
Inp 704.00 NIST
Inp 710.00 NIST
Inp 750.00 NIST
Inp 734.00 NIST
Inp 750.00 NIST
Inp 740.00 NIST
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Inp 717.00 NIST
Inp 718.00 NIST
Inp 719.00 NIST
Inp 719.00 NIST
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Inp 724.00 NIST
Inp 714.00 NIST
Inp 722.00 NIST
Inp 717.00 NIST
Inp 736.00 NIST
Inp 719.00 NIST
Inp 743.00 NIST
Inp 716.00 NIST
Inp 715.00 NIST
Inp 728.00 NIST
Inp 722.00 NIST
Inp 723.00 NIST
Inp Outlier 760.00 NIST
Inp 747.00 NIST
Inp 734.10 NIST
Inp 747.00 NIST
Inp 732.00 NIST
Inp 740.00 NIST
Inp 721.00 NIST
Inp 732.00 NIST
Inp 748.00 NIST
Inp 733.00 NIST
Inp 726.00 NIST
Inp 726.00 NIST
Inp 732.00 NIST
Inp 737.00 NIST
Inp 729.00 NIST
Inp 726.00 NIST
Inp 734.00 NIST
Inp 726.00 NIST
Inp 734.00 NIST
Inp 739.00 NIST
Inp Outlier 773.00 NIST
Inp 739.00 NIST
Inp 726.00 NIST
Inp 725.00 NIST
Inp 719.00 NIST
Inp 709.00 NIST
Inp 727.00 NIST
Inp 735.00 NIST
Inp 742.00 NIST
Inp 717.00 NIST
Inp 741.00 NIST
Inp 730.00 NIST
Inp 737.00 NIST
Inp 741.00 NIST
Inp 749.00 NIST
Inp 718.00 NIST
Inp 739.00 NIST
Inp 736.00 NIST
Inp 735.00 NIST
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Inp 745.00 NIST
Inp 727.00 NIST
Inp 727.00 NIST
Inp 736.00 NIST
Inp 735.00 NIST
Inp 734.00 NIST
Inp 737.00 NIST
Inp Outlier 759.30 NIST
Inp 734.00 NIST
Inp 736.00 NIST
Inp 731.00 NIST
Inp 731.00 NIST
Inp 732.00 NIST
Inp 715.00 NIST
Inp 729.00 NIST
Inp 746.00 NIST
Inp Outlier 773.00 NIST
Inp 749.00 NIST
Inp 720.00 NIST
Inp 735.00 NIST
Inp 717.00 NIST
Inp 718.00 NIST
Inp 738.00 NIST
Inp 736.00 NIST
Inp 730.00 NIST
Inp 731.00 NIST
Inp 727.00 NIST
Inp 734.00 NIST
Inp 736.00 NIST
Inp 736.00 NIST
Inp 726.00 NIST
Inp 721.81 NIST
Inp 753.00 NIST
Inp 718.00 NIST
Inp 734.00 NIST
Inp 753.00 NIST
Inp 731.00 NIST
Inp 737.00 NIST
Inp 717.00 NIST
Inp 717.00 NIST
Inp 726.00 NIST
Inp 714.00 NIST
Inp 736.00 NIST
Inp 736.00 NIST
Inp 714.00 NIST
Inp 739.00 NIST
Inp 710.00 NIST
Inp 720.00 NIST
Inp 713.00 NIST
Inp 720.00 NIST
Inp 714.00 NIST
Inp 716.00 NIST
Inp 719.00 NIST
Inp 743.00 NIST
Inp 719.00 NIST
Inp 714.00 NIST
Inp 714.00 NIST
Inp 734.00 NIST
Inp 714.00 NIST
Inp 716.00 NIST
Inp 737.00 NIST
Inp 728.00 NIST
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Inp 735.00 NIST
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Inp 705.00 NIST
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Inp 755.00 NIST
Inp 729.00 NIST
Inp 755.00 NIST
Inp 707.00 NIST
Inp 710.00 NIST
Inp 741.00 NIST
Inp 707.00 NIST
Inp Outlier 768.00 NIST
Inp 736.00 NIST
Inp 715.00 NIST
Inp 736.00 NIST
Inp 736.00 NIST
Inp 732.00 NIST
Inp 744.00 NIST
Inp 745.00 NIST
Inp 718.00 NIST
Inp 713.00 NIST
Inp 725.00 NIST
Inp 731.00 NIST
Inp 738.00 NIST
Inp 737.00 NIST
Inp 707.00 NIST
Inp 707.00 NIST
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Inp 719.00 NIST
Inp 741.00 NIST
Inp 736.00 NIST
Inp 742.00 NIST
Inp 715.00 NIST
Inp 735.00 NIST
Inp 736.00 NIST
Inp 727.00 NIST
Inp 739.00 NIST
Inp 719.00 NIST
Inp 738.00 NIST
Inp 738.00 NIST
Inp Outlier 758.00 NIST
Inp Outlier 767.00 NIST
Inp 720.00 NIST
Inp 719.00 NIST
Inp 732.00 NIST
Inp 726.00 NIST
Inp 737.00 NIST
Inp 744.00 NIST
Inp 719.00 NIST
Inp 710.00 NIST
Inp 719.00 NIST
Inp 737.00 NIST
Inp 742.00 NIST
Inp 737.00 NIST
Inp 742.00 NIST
Inp Outlier 772.00 NIST
Inp 711.00 NIST
Inp 713.00 NIST
Inp 724.00 NIST
Inp 719.00 NIST
Inp 706.00 NIST
Inp 718.00 NIST
Inp 719.00 NIST
Inp 736.00 NIST
Inp 736.00 NIST
Inp 738.00 NIST
Inp 748.00 NIST
Inp 730.00 NIST
Inp 748.00 NIST
Inp 719.00 NIST
Inp 720.00 NIST
Inp 714.00 NIST
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Inp 714.00 NIST
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Inp 719.00 NIST
Inp 749.00 NIST
Inp 716.00 NIST
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Inp 709.00 NIST
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Inp 745.00 NIST
Inp 734.00 NIST
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Inp 737.00 NIST
Ip [1159.00; 1255.00]   Show Hide
Ip 1208.00 NIST
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Ip 1212.00 NIST
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Ip 1238.00 NIST
Ip 1212.00 NIST
Ip 1203.00 NIST
Ip Outlier 1240.00 NIST
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Ip 1200.00 NIST
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Ip 1211.00 NIST
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Ip 1180.00 NIST
Ip Outlier 1174.00 NIST
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Ip 1237.00 NIST
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Ip 1223.00 NIST
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Ip 1194.00 NIST
Ip 1199.00 NIST
Ip Outlier 1163.00 NIST
Ip Outlier 1165.00 NIST
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Ip 1214.00 NIST
Ip 1223.00 NIST
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Ip 1200.00 NIST
Ip 1206.00 NIST
Ip Outlier 1163.00 NIST
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Ip 1190.00 NIST
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Ip Outlier 1255.00 NIST
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Ip Outlier 1250.00 NIST
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Ip 1203.00 NIST
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Ip 1213.00 NIST
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Ip 1229.60 NIST
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Ip 1210.00 NIST
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Ip Outlier 1172.00 NIST
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Ip Outlier 1247.00 NIST
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Ip 1229.00 NIST
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Ip Outlier 1168.00 NIST
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Ip 1200.00 NIST
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Ip Outlier 1174.00 NIST
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Ip Outlier 1174.00 NIST
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Ip Outlier 1159.00 NIST
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Tboil [401.15; 433.30] K Show Hide
Tboil 404.50 K Phase equilibria of (water + levunilic acid + alcohol) ternary systems
Tboil 404.90 K Vapor liquid equilibrium of the ethanol + 3-methyl-1-butanol system at 50.66, 101.33 and 151.99 kPa
Tboil 404.55 K (Liquid + liquid) equilibria of (water + butyric acid + isoamyl alcohol) ternary system
Tboil 404.45 K Effect of Pressure on the Azeotrope of the Mixture Isoamyl Acetate Isoamyl Alcohol at 50.00, 101.32, 250.00, and 350.00 kPa
Tboil 404.27 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 404.20 K KDB
Tboil 403.53 ± 0.25 K NIST
Tboil 403.20 K NIST
Tboil 403.91 ± 0.03 K NIST
Tboil Outlier 433.30 ± 0.20 K NIST
Tboil 404.20 K NIST
Tboil 403.75 ± 0.30 K NIST
Tboil 404.35 ± 0.30 K NIST
Tboil 404.90 ± 0.50 K NIST
Tboil 402.70 ± 0.40 K NIST
Tboil 405.20 ± 0.50 K NIST
Tboil 405.20 ± 0.50 K NIST
Tboil 405.00 ± 1.00 K NIST
Tboil 405.15 ± 1.50 K NIST
Tboil 403.95 K NIST
Tboil 405.15 ± 0.30 K NIST
Tboil 405.20 ± 0.40 K NIST
Tboil 405.00 ± 0.50 K NIST
Tboil 404.49 ± 0.15 K NIST
Tboil 405.05 ± 0.50 K NIST
Tboil 403.15 ± 2.00 K NIST
Tboil 405.15 ± 0.50 K NIST
Tboil 405.05 ± 0.30 K NIST
Tboil 404.95 ± 0.50 K NIST
Tboil 404.85 ± 0.50 K NIST
Tboil 404.65 ± 1.00 K NIST
Tboil 404.75 ± 0.50 K NIST
Tboil 405.05 ± 0.50 K NIST
Tboil 403.65 ± 2.00 K NIST
Tboil 405.10 ± 0.50 K NIST
Tboil 405.10 ± 0.60 K NIST
Tboil 404.65 ± 0.50 K NIST
Tboil 402.00 ± 3.00 K NIST
Tboil 405.15 ± 2.00 K NIST
Tboil 403.15 ± 2.00 K NIST
Tboil 403.15 ± 2.00 K NIST
Tboil 402.65 ± 2.00 K NIST
Tboil 404.15 ± 2.00 K NIST
Tboil 404.75 ± 0.70 K NIST
Tboil 403.65 ± 1.00 K NIST
Tboil 403.65 ± 1.00 K NIST
Tboil 403.85 ± 0.50 K NIST
Tboil 404.05 ± 0.50 K NIST
Tboil 401.15 ± 3.00 K NIST
Tboil 401.15 ± 3.00 K NIST
Tboil 403.40 ± 1.00 K NIST
Tboil 403.70 ± 2.00 K NIST
Tboil 405.15 ± 0.40 K NIST
Tboil 404.15 ± 2.00 K NIST
Tboil 405.15 ± 0.20 K NIST
Tboil 404.00 ± 0.40 K NIST
Tboil 404.15 ± 1.00 K NIST
Tboil 404.60 ± 0.50 K NIST
Tboil 404.50 ± 0.50 K NIST
Tboil 404.50 ± 0.50 K NIST
Tboil 405.20 ± 0.30 K NIST
Tboil 405.20 ± 0.50 K NIST
Tboil 404.40 ± 1.00 K NIST
Tboil 404.70 ± 0.50 K NIST
Tboil 404.50 ± 0.50 K NIST
Tboil 404.45 ± 0.30 K NIST
Tboil 404.50 ± 0.20 K NIST
Tboil 403.15 ± 1.00 K NIST
Tboil 406.00 ± 5.00 K NIST
Tboil 404.00 ± 0.50 K NIST
Tboil 404.30 ± 0.50 K NIST
Tboil 404.65 ± 1.00 K NIST
Tboil 404.35 ± 0.50 K NIST
Tboil 404.75 ± 0.50 K NIST
Tboil 403.90 ± 1.50 K NIST
Tboil 404.65 ± 2.00 K NIST
Tboil 401.65 ± 3.00 K NIST
Tboil 404.55 ± 0.50 K NIST
Tboil 401.15 ± 3.00 K NIST
Tboil 404.75 ± 0.20 K NIST
Tboil 402.65 ± 2.00 K NIST
Tboil 404.65 ± 2.00 K NIST
Tboil 404.15 ± 2.00 K NIST
Tboil 404.00 ± 2.00 K NIST
Tboil 404.65 ± 1.00 K NIST
Tboil 405.20 ± 2.00 K NIST
Tboil 403.26 ± 1.00 K NIST
Tboil 402.85 ± 1.50 K NIST
Tboil 404.65 ± 2.00 K NIST
Tboil 405.65 ± 3.00 K NIST
Tboil 402.15 ± 3.00 K NIST
Tc [577.20; 582.90] K Show Hide
Tc 577.20 K IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Tc 579.50 K PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc 577.20 K KDB
Tc 577.20 ± 0.50 K NIST
Tc 577.20 ± 0.70 K NIST
Tc 579.40 K NIST
Tc 580.15 ± 1.00 K NIST
Tc 579.20 ± 0.35 K NIST
Tc 580.40 K NIST
Tc Outlier 582.90 K NIST
Tc 579.20 K NIST
Tc 579.80 K NIST
Tfus [155.90; 156.15] K Show Hide
Tfus 156.15 K Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus 155.90 K KDB
Tfus 156.08 K Aq. Solubility Prediction
Ttriple 118.00 K Heat Capacities in the Solid and in the Liquid Phase of Isomeric Pentanols
Vc 0.329 m3/kmol PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,gas [187.20; 200.70] J/mol×K [451.65; 499.15] Show Hide
Cp,gas 187.20 ± 1.10 J/mol×K 451.65 NIST
Cp,gas 193.70 ± 1.10 J/mol×K 474.55 NIST
Cp,gas 197.60 ± 1.10 J/mol×K 488.35 NIST
Cp,gas 200.70 ± 1.10 J/mol×K 499.15 NIST
Cp,liquid [209.52; 257.70] J/mol×K [295.52; 347.00] Show Hide
Cp,liquid 209.52 J/mol×K 295.52 NIST
Cp,liquid 210.00 J/mol×K 303.00 NIST
Cp,liquid 257.70 J/mol×K 347.00 NIST
ΔvapH [44.07; 57.10] kJ/mol [303.00; 404.20] Show Hide
ΔvapH 55.20 ± 0.20 kJ/mol 303.00 NIST
ΔvapH 54.20 ± 0.20 kJ/mol 313.00 NIST
ΔvapH 52.90 ± 0.20 kJ/mol 328.00 NIST
ΔvapH 51.40 ± 0.20 kJ/mol 343.00 NIST
ΔvapH 47.20 kJ/mol 355.00 NIST
ΔvapH 57.10 kJ/mol 357.50 NIST
ΔvapH 49.70 ± 0.20 kJ/mol 358.00 NIST
ΔvapH 56.50 kJ/mol 362.00 NIST
ΔvapH 49.80 kJ/mol 376.00 NIST
ΔvapH 44.07 kJ/mol 404.20 NIST
ν [0.0000023; 0.0000050] m2/s [293.15; 323.15] Show Hide
ν 0.0000050 m2/s 293.15 Density, Viscosity, Excess Molar Volume, and Viscosity Deviation of Three Amyl Alcohols + Ethanol Binary Mixtures from 293.15 to 323.15 K
ν 0.0000044 m2/s 298.15 Density, Viscosity, Excess Molar Volume, and Viscosity Deviation of Three Amyl Alcohols + Ethanol Binary Mixtures from 293.15 to 323.15 K
ν 0.0000038 m2/s 303.15 Density, Viscosity, Excess Molar Volume, and Viscosity Deviation of Three Amyl Alcohols + Ethanol Binary Mixtures from 293.15 to 323.15 K
ν 0.0000033 m2/s 308.15 Density, Viscosity, Excess Molar Volume, and Viscosity Deviation of Three Amyl Alcohols + Ethanol Binary Mixtures from 293.15 to 323.15 K
ν 0.0000029 m2/s 313.15 Density, Viscosity, Excess Molar Volume, and Viscosity Deviation of Three Amyl Alcohols + Ethanol Binary Mixtures from 293.15 to 323.15 K
ν 0.0000026 m2/s 318.15 Density, Viscosity, Excess Molar Volume, and Viscosity Deviation of Three Amyl Alcohols + Ethanol Binary Mixtures from 293.15 to 323.15 K
ν 0.0000023 m2/s 323.15 Density, Viscosity, Excess Molar Volume, and Viscosity Deviation of Three Amyl Alcohols + Ethanol Binary Mixtures from 293.15 to 323.15 K
Pvap [15.00; 176.50] kPa [357.50; 422.40] Show Hide
Pvap 15.00 kPa 357.50 Complementary vapor pressure data for 2-methyl-1-propanol and 3-methyl-1-butanol at a pressure range of (15 to 177) kPa
Pvap 22.66 kPa 366.27 Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap 23.50 kPa 367.20 Complementary vapor pressure data for 2-methyl-1-propanol and 3-methyl-1-butanol at a pressure range of (15 to 177) kPa
Pvap 26.66 kPa 369.95 Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap 30.66 kPa 373.24 Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap 32.00 kPa 374.40 Complementary vapor pressure data for 2-methyl-1-propanol and 3-methyl-1-butanol at a pressure range of (15 to 177) kPa
Pvap 34.66 kPa 376.14 Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap 40.00 kPa 379.65 Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap 40.50 kPa 380.10 Complementary vapor pressure data for 2-methyl-1-propanol and 3-methyl-1-butanol at a pressure range of (15 to 177) kPa
Pvap 45.33 kPa 382.78 Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap 49.00 kPa 384.80 Complementary vapor pressure data for 2-methyl-1-propanol and 3-methyl-1-butanol at a pressure range of (15 to 177) kPa
Pvap 50.66 kPa 385.62 Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap 55.99 kPa 388.23 Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap 57.50 kPa 389.10 Complementary vapor pressure data for 2-methyl-1-propanol and 3-methyl-1-butanol at a pressure range of (15 to 177) kPa
Pvap 61.33 kPa 390.64 Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap 66.00 kPa 392.80 Complementary vapor pressure data for 2-methyl-1-propanol and 3-methyl-1-butanol at a pressure range of (15 to 177) kPa
Pvap 66.66 kPa 392.88 Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap 73.33 kPa 395.48 Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap 79.99 kPa 397.90 Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap 86.66 kPa 400.18 Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap 91.50 kPa 402.00 Complementary vapor pressure data for 2-methyl-1-propanol and 3-methyl-1-butanol at a pressure range of (15 to 177) kPa
Pvap 93.33 kPa 402.32 Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap 97.99 kPa 403.77 Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 2
Pvap 108.50 kPa 407.00 Complementary vapor pressure data for 2-methyl-1-propanol and 3-methyl-1-butanol at a pressure range of (15 to 177) kPa
Pvap 117.00 kPa 409.30 Complementary vapor pressure data for 2-methyl-1-propanol and 3-methyl-1-butanol at a pressure range of (15 to 177) kPa
Pvap 125.50 kPa 411.40 Complementary vapor pressure data for 2-methyl-1-propanol and 3-methyl-1-butanol at a pressure range of (15 to 177) kPa
Pvap 134.00 kPa 413.50 Complementary vapor pressure data for 2-methyl-1-propanol and 3-methyl-1-butanol at a pressure range of (15 to 177) kPa
Pvap 142.50 kPa 415.40 Complementary vapor pressure data for 2-methyl-1-propanol and 3-methyl-1-butanol at a pressure range of (15 to 177) kPa
Pvap 151.00 kPa 417.30 Complementary vapor pressure data for 2-methyl-1-propanol and 3-methyl-1-butanol at a pressure range of (15 to 177) kPa
Pvap 159.50 kPa 419.20 Complementary vapor pressure data for 2-methyl-1-propanol and 3-methyl-1-butanol at a pressure range of (15 to 177) kPa
Pvap 168.00 kPa 420.90 Complementary vapor pressure data for 2-methyl-1-propanol and 3-methyl-1-butanol at a pressure range of (15 to 177) kPa
Pvap 176.50 kPa 422.40 Complementary vapor pressure data for 2-methyl-1-propanol and 3-methyl-1-butanol at a pressure range of (15 to 177) kPa
n0 [1.37820; 1.45010]   [293.15; 308.15] Show Hide
n0 1.40540 293.15 Isobaric Vapor - Liquid Equilibria for the Ternary System of 2-Methyl-1-butanol, 3-Methyl-1-butanol, and Ethylene Glycol at 101.3 kPa
n0 1.41300 293.15 Liquid Liquid Equilibrium for the Ternary System 2-Methyl-1-propanol + 3-Methyl-1-butanol + Water at (298.15, 323.15, and 348.15) K
n0 1.40750 293.15 Distribution of Butyric Acid between Water and Several Solvents
n0 1.40500 298.15 Thermodynamic properties of (tetradecane + benzene, + toluene, + chlorobenzene, + bromobenzene, + anisole) binary mixtures at T = (298.15, 303.15, and 308.15) K
n0 1.40515 298.15 Density, Refractive Index, Speed of Sound at 298.15 K, and Vapor-Liquid Equilibria at 101.3 kPa for Binary Mixtures of Propanol + 2-Methyl-1-butanol and Propanol + 3-Methyl-1-butanol
n0 1.45010 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 1.40470 298.15 Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures of Diisopropyl Ether, 2-Propyl Alcohol, and 3-Methyl-1-Butanol
n0 1.40530 298.15 Excess volumes and excess enthalpies of N-methyl-2-pyrrolidone with branched alcohols
n0 1.40500 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 1.40510 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 1.40560 298.15 Physico-chemical and excess properties of the binary mixtures of methylcyclohexane + ethanol, + propan-1-ol, + propan-2-ol, + butan-1-ol, + 2-methyl-1-propanol, or 3-methyl-1-butanol at T = (298.15, 303.15, and 308.15) K
n0 1.40530 298.15 Isobaric (vapour + liquid) equilibrium for N-methyl-2-pyrrolidone with branched alcohols
n0 1.40300 298.15 Experimental Binary VLE Data of Morpholine with 1-Butanol and 3-Methyl-1-butanol Systems
n0 1.40420 298.15 Isobaric Vapor Liquid Equilibrium for Binary and Ternary Systems of Isoamyl Alcohol + Isoamyl Acetate + Dimethyl Sulfoxide at 101.33 kPa
n0 1.40850 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 1.40340 303.15 Physico-chemical and excess properties of the binary mixtures of methylcyclohexane + ethanol, + propan-1-ol, + propan-2-ol, + butan-1-ol, + 2-methyl-1-propanol, or 3-methyl-1-butanol at T = (298.15, 303.15, and 308.15) K
n0 1.40300 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 1.40300 303.15 Thermodynamic properties of (tetradecane + benzene, + toluene, + chlorobenzene, + bromobenzene, + anisole) binary mixtures at T = (298.15, 303.15, and 308.15) K
n0 1.40350 303.15 Densities, Viscosities, Sound Speeds, Refractive Indices, and Excess Properties of Binary Mixtures of Isoamyl Alcohol with Some Alkoxyethanols
n0 1.40130 308.15 Physico-chemical and excess properties of the binary mixtures of methylcyclohexane + ethanol, + propan-1-ol, + propan-2-ol, + butan-1-ol, + 2-methyl-1-propanol, or 3-methyl-1-butanol at T = (298.15, 303.15, and 308.15) K
n0 1.37820 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 1.40100 308.15 Thermodynamic properties of (tetradecane + benzene, + toluene, + chlorobenzene, + bromobenzene, + anisole) binary mixtures at T = (298.15, 303.15, and 308.15) K
ρl [778.14; 812.29] kg/m3 [288.15; 332.70] Show Hide
ρl 812.29 kg/m3 288.15 Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl 810.00 kg/m3 293.00 KDB
ρl 808.58 kg/m3 293.15 Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl 804.43 kg/m3 293.20 Liquid-liquid equilibrium data and thermophysical properties for ternary systems composed of water, acetic acid and different solvents
ρl 804.84 kg/m3 298.15 Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl 806.21 kg/m3 298.15 Vapor Liquid Equilibrium of Mixtures Containing the Following Higher Alcohols: 2-Propanol, 2-Methyl-1-propanol, and 3-Methyl-1-butanol
ρl 804.24 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 811.04 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 807.16 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 807.16 kg/m3 298.15 Dielectric study of H-bonded interactions in amyl alcohols with ketones and DMSO at T = 298.15 K
ρl 807.30 kg/m3 298.15 Isobaric Vapor Liquid Equilibrium for Two Binary Systems, (3-Methyl-1-butanol + 1,4-Butanediol) and (Hexylene Glycol + 1,4-Butanediol), at p = 40.0, 60.0, and 80.0 kPa
ρl 808.94 kg/m3 298.20 Isothermal vapor-liquid equilibria, excess molar volume and the deviation of refractive indices for binary mixtures of 1-butanol, 1- hexanol, 3-methyl-1-butanol and butyl acetate
ρl 807.16 kg/m3 298.20 Modeling phase equilibria of ternary systems (water + formic acid + ester or alcohol) through UNIFAC-original, SERLAS, NRTL, NRTL-modified, and three-suffix Margules: Parameter estimation using genetic algorithm
ρl 803.20 kg/m3 303.15 Viscous synergy and antagonism and isentropic compressibility of ternary mixtures containing 1,3-dioxolane, water and monoalkanols at 303.15K
ρl 801.09 kg/m3 303.15 Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl 796.95 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 797.31 kg/m3 308.15 Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl 793.51 kg/m3 313.15 Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl 794.43 kg/m3 313.20 Liquid-liquid equilibrium data and thermophysical properties for ternary systems composed of water, acetic acid and different solvents
ρl 789.67 kg/m3 318.15 Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl 785.79 kg/m3 323.15 Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl 778.14 kg/m3 332.70 Isothermal vapor liquid equilibria for different binary mixtures involved in the alcoholic distillation
γ [0.02; 0.02] N/m [293.15; 328.15] Show Hide
γ 0.02 N/m 293.15 Surface Tensions of Three Amyl Alcohol + Ethanol Binary Mixtures from (293.15 to 323.15) K
γ 0.02 N/m 298.15 Equilibrium surface tension and the interaction energy of DMSO with tert-butyl alcohol or iso-amyl alcohol at various temperatures
γ 0.02 N/m 298.15 Surface Tensions of Three Amyl Alcohol + Ethanol Binary Mixtures from (293.15 to 323.15) K
γ 0.02 N/m 303.15 Surface Tensions of Three Amyl Alcohol + Ethanol Binary Mixtures from (293.15 to 323.15) K
γ 0.02 N/m 308.15 Equilibrium surface tension and the interaction energy of DMSO with tert-butyl alcohol or iso-amyl alcohol at various temperatures
γ 0.02 N/m 308.15 Surface Tensions of Three Amyl Alcohol + Ethanol Binary Mixtures from (293.15 to 323.15) K
γ 0.02 N/m 313.15 Surface Tensions of Three Amyl Alcohol + Ethanol Binary Mixtures from (293.15 to 323.15) K
γ 0.02 N/m 318.15 Equilibrium surface tension and the interaction energy of DMSO with tert-butyl alcohol or iso-amyl alcohol at various temperatures
γ 0.02 N/m 318.15 Surface Tensions of Three Amyl Alcohol + Ethanol Binary Mixtures from (293.15 to 323.15) K
γ 0.02 N/m 323.15 Surface Tensions of Three Amyl Alcohol + Ethanol Binary Mixtures from (293.15 to 323.15) K
γ 0.02 N/m 328.15 Equilibrium surface tension and the interaction energy of DMSO with tert-butyl alcohol or iso-amyl alcohol at various temperatures

Correlations

Property Value Unit Temperature (K) Source
η [6.2960233; 0.0002851] Pa×s [156.04; 405.14] Joback Predicted correlation Show Hide
EquationY = exp(A + B/T + C·ln(T) + D·T^E)
Y is η in Pa×s, T in K
Coefficient A-1.44290e+01
Coefficient B2.53865e+03
Coefficient C0.00000e+00
Coefficient D0.00000e+00
Coefficient E0.00000e+00
CommentLiquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc.
Temperature range, min.156.04
Temperature range, max.405.14
η 6.2960233 Pa×s 156.04 Calculated Property
η 0.5428303 Pa×s 183.72 Calculated Property
η 0.0889149 Pa×s 211.40 Calculated Property
η 0.0221412 Pa×s 239.07 Calculated Property
η 0.0073573 Pa×s 266.75 Calculated Property
η 0.0030074 Pa×s 294.43 Calculated Property
η 0.0014336 Pa×s 322.11 Calculated Property
η 0.0007684 Pa×s 349.78 Calculated Property
η 0.0004513 Pa×s 377.46 Calculated Property
η 0.0002851 Pa×s 405.14 Calculated Property
Property Value Unit Temperature (K) Source
Pvap [1.33; 202.65] kPa [317.06; 425.73] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.42576e+01
Coefficient B-2.70339e+03
Coefficient C-1.23544e+02
Temperature range, min.317.06
Temperature range, max.425.73
Pvap 1.33 kPa 317.06 Calculated Property
Pvap 3.03 kPa 329.13 Calculated Property
Pvap 6.28 kPa 341.21 Calculated Property
Pvap 12.07 kPa 353.28 Calculated Property
Pvap 21.71 kPa 365.36 Calculated Property
Pvap 36.95 kPa 377.43 Calculated Property
Pvap 59.92 kPa 389.51 Calculated Property
Pvap 93.17 kPa 401.58 Calculated Property
Pvap 139.65 kPa 413.66 Calculated Property
Pvap 202.65 kPa 425.73 Calculated Property
Pvap [8.90e-11; 3843.71] kPa [161.00; 579.45] 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 A1.12297e+02
Coefficient B-1.06664e+04
Coefficient C-1.36325e+01
Coefficient D3.26511e-06
Coefficient E0.00000e+00
Temperature range, min.161.00
Temperature range, max.579.45
Pvap 8.90e-11 kPa 161.00 Calculated Property
Pvap 8.30e-06 kPa 207.49 Calculated Property
Pvap 6.91e-03 kPa 253.99 Calculated Property
Pvap 0.50 kPa 300.48 Calculated Property
Pvap 9.11 kPa 346.98 Calculated Property
Pvap 69.37 kPa 393.47 Calculated Property
Pvap 301.32 kPa 439.97 Calculated Property
Pvap 894.68 kPa 486.46 Calculated Property
Pvap 2037.91 kPa 532.96 Calculated Property
Pvap 3843.71 kPa 579.45 Calculated Property
Property Value Unit Temperature (K) Source
γ [0.04; 0.02] N/m [156.15; 404.15] Jasper (1972), surface tension of pure liquid compounds Compiled value Show Hide
EquationY = A + B·T + C·T² + D·T³ + E·T⁴
Y is γ in N/m, T in K
Coefficient A4.81583e-02
Coefficient B-8.20000e-05
Coefficient C0.00000e+00
Coefficient D0.00000e+00
Coefficient E0.00000e+00
Temperature range, min.156.15
Temperature range, max.404.15
γ 0.04 N/m 156.15 Calculated Property
γ 0.03 N/m 183.71 Calculated Property
γ 0.03 N/m 211.26 Calculated Property
γ 0.03 N/m 238.82 Calculated Property
γ 0.03 N/m 266.37 Calculated Property
γ 0.02 N/m 293.93 Calculated Property
γ 0.02 N/m 321.48 Calculated Property
γ 0.02 N/m 349.04 Calculated Property
γ 0.02 N/m 376.59 Calculated Property
γ 0.02 N/m 404.15 Calculated Property

Similar Compounds

(S)-(+)-3-Methyl-1-pentanol. 1-Pentanol, 3-methyl-. 1,5-Pentanediol, 3-methyl-. 1,4-Butanediol, 2-methyl-. 1-Pentanol, 3,4-dimethyl-. 1-Hexanol, 3-methyl-. (S)-3-Ethyl-4-methylpentanol. 3-Ethyl-4-methylpentan-1-ol. 1-Heptanol, 3-methyl-. 1-Dodecanol, 3,7,11-trimethyl-. 1-Octanol, 3,7-dimethyl-, (R)-. 1-Hexadecanol, 3,7,11,15-tetramethyl-. 1-Octanol, 3,7-dimethyl-, (S)-. 1-Octanol, 3,7-dimethyl-. 2-methylbutanol-d-9.

Find more compounds similar to 1-Butanol, 3-methyl-.

Mixtures

Find more mixtures with 1-Butanol, 3-methyl-.

Sources

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