Chemical Properties of 1-Propanol, 2-methyl- (CAS 78-83-1)

1-Propanol, 2-methyl-

InChI
InChI=1S/C4H10O/c1-4(2)3-5/h4-5H,3H2,1-2H3
InChI Key
ZXEKIIBDNHEJCQ-UHFFFAOYSA-N
Formula
C4H10O
SMILES
CC(C)CO
Molecular Weight1
74.12
CAS
78-83-1
Other Names
  • 1-Hydroxymethylpropane
  • 2-Methylpropanol
  • 2-Methylpropanol-1
  • 2-Methylpropyl alcohol
  • 2-methyl-1-propanol
  • 2-methyl-1-propanyl alcohol
  • 2-methylpropan-1-ol
  • 2-methylpropanoI
  • Alcool isobutylique
  • Butanol-iso
  • Fermentation butyl alcohol
  • Isobutylalkohol
  • Isopropyl carbitol
  • Isopropylcarbinol
  • Methyl-2 propanol-1
  • NSC 5708
  • Propanol, 2-methyl-
  • Rcra waste number U140
  • UN 1212
  • i-Butanol
  • i-Butyl alcohol
  • iso-C4H9OH
  • isobutanol
  • isobutyl alcohol
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Contents

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

Physical Properties

Property Value Unit Source
ω [0.5880; 0.5920]   Show Hide
ω 0.5880 PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω 0.5900 ChemSep v8.3 pure component data Compiled value
ω 0.5920 KDB
PAff 793.70 kJ/mol NIST
Tig [688.15; 699.82] K Show Hide
Tig 699.82 K KDB
Tig 688.15 K NCMS SOLV-DB
BasG 762.20 kJ/mol NIST
ΔcH°liquid [-2669.60; -2665.79] kJ/mol Show Hide
ΔcH°liquid -2669.60 ± 0.59 kJ/mol NIST
ΔcH°liquid -2668.50 ± 0.84 kJ/mol NIST
ΔcH°liquid -2665.79 kJ/mol NIST
Cp,liquid 181.90 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 [1.64; 1.70] debye Show Hide
μ 1.64 debye ChemSep v8.3 pure component data Compiled value
μ 1.70 debye KDB
η [0.0033070; 0.0034040] Pa×s Show Hide
η 0.0033070 Pa×s Thermodynamic properties of binary liquid mixtures of diethylenetriamine with alcohols at different temperatures
η 0.0034040 Pa×s Thermophysical Properties of Binary Mixtures of 2-Methyl-1-propanol with Hexane, Octane, and Decane at 298.15 K
εr 17.93 NCMS SOLV-DB
LFL 1.60 % in Air KDB
UFL 10.90 % in Air KDB
Tflash,cc [301.15; 305.37] K Show Hide
Tflash,cc 305.37 K KDB
Tflash,cc 301.15 K NCMS SOLV-DB
Tflash,oc 300.93 K KDB
ΔfG° [-167.40; -154.90] kJ/mol Show Hide
ΔfG° -154.90 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfG° -167.40 kJ/mol KDB
Rg 3.1400 KDB
ΔfH°gas [-284.00; -282.90] kJ/mol Show Hide
ΔfH°gas -283.20 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfH°gas -283.40 kJ/mol KDB
ΔfH°gas -283.80 ± 0.90 kJ/mol NIST
ΔfH°gas -282.90 kJ/mol NIST
ΔfH°gas -284.00 ± 1.50 kJ/mol NIST
ΔfH°liquid [-334.70; -333.60] kJ/mol Show Hide
ΔfH°liquid -334.60 ± 0.90 kJ/mol NIST
ΔfH°liquid -333.60 ± 0.63 kJ/mol NIST
ΔfH°liquid -334.70 ± 0.84 kJ/mol NIST
ΔfusH° 6.68 kJ/mol Joback Calculated Property
ΔvapH° [42.89; 50.89] kJ/mol Show Hide
ΔvapH° 50.79 kJ/mol NCMS SOLV-DB
ΔvapH° 50.89 kJ/mol NIST
ΔvapH° 48.80 kJ/mol NIST
ΔvapH° 50.76 ± 0.03 kJ/mol NIST
ΔvapH° 50.80 ± 0.10 kJ/mol NIST
ΔvapH° 50.80 kJ/mol NIST
ΔvapH° 50.79 ± 0.02 kJ/mol NIST
ΔvapH° 50.80 ± 0.10 kJ/mol NIST
ΔvapH° 50.84 ± 0.08 kJ/mol NIST
ΔvapH° 49.80 kJ/mol NIST
ΔvapH° 50.70 kJ/mol NIST
ΔvapH° Outlier 42.89 ± 0.01 kJ/mol NIST
IE [10.02; 10.47] eV Show Hide
IE 10.02 ± 0.02 eV NIST
IE 10.02 ± 0.05 eV NIST
IE 10.11 ± 0.07 eV NIST
IE 10.12 ± 0.04 eV NIST
IE 10.09 ± 0.02 eV NIST
IE Outlier 10.47 ± 0.03 eV NIST
log10WS [0.04; 0.10]   Show Hide
log10WS 0.04 Aq. Solubility Prediction
log10WS 0.10 Estimated Solubility
logPoct/wat 0.760 NCMS SOLV-DB
McVol 73.090 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 [4294.00; 4891.00] kPa Show Hide
Pc 4295.00 kPa IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Pc 4296.18 kPa PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc 4300.00 kPa ChemSep v8.3 pure component data Compiled value
Pc 4295.00 kPa KDB
Pc 4300.00 ± 20.00 kPa NIST
Pc 4320.00 kPa NIST
Pc 4295.00 kPa NIST
Pc 4294.00 kPa NIST
Pc 4863.60 ± 101.32 kPa NIST
Pc Outlier 4891.00 kPa NIST
Ptriple 2.46e-09 kPa ChemSep v8.3 pure component data Compiled value
ρc [269.06; 272.17] kg/m3 Show Hide
ρc 271.29 ± 1.48 kg/m3 NIST
ρc 272.17 kg/m3 NIST
ρc 269.06 kg/m3 NIST
Inp [580.00; 663.00]   Show Hide
Inp 596.00 NIST
Inp 617.93 NIST
Inp 629.00 NIST
Inp 629.00 NIST
Inp 609.00 NIST
Inp 629.00 NIST
Inp 641.00 NIST
Inp 620.00 NIST
Inp 629.00 NIST
Inp 609.00 NIST
Inp 629.00 NIST
Inp 641.00 NIST
Inp 620.00 NIST
Inp 629.00 NIST
Inp 609.00 NIST
Inp 605.00 NIST
Inp 601.00 NIST
Inp Outlier 586.00 NIST
Inp 595.00 NIST
Inp Outlier 584.00 NIST
Inp Outlier 585.00 NIST
Inp 612.00 NIST
Inp 609.00 NIST
Inp 589.00 NIST
Inp Outlier 580.00 NIST
Inp 612.00 NIST
Inp 648.00 NIST
Inp 607.00 NIST
Inp 608.00 NIST
Inp 636.00 NIST
Inp 637.00 NIST
Inp 612.00 NIST
Inp 616.00 NIST
Inp 594.60 NIST
Inp 637.00 NIST
Inp 645.00 NIST
Inp 646.00 NIST
Inp 629.00 NIST
Inp Outlier 654.00 NIST
Inp 622.00 NIST
Inp 629.00 NIST
Inp 622.00 NIST
Inp 626.00 NIST
Inp 624.70 NIST
Inp 626.10 NIST
Inp 590.00 NIST
Inp 621.20 NIST
Inp 592.00 NIST
Inp 609.00 NIST
Inp 617.00 NIST
Inp 592.00 NIST
Inp 644.00 NIST
Inp 627.00 NIST
Inp 611.00 NIST
Inp 611.00 NIST
Inp 611.00 NIST
Inp 612.00 NIST
Inp 609.00 NIST
Inp 609.00 NIST
Inp 612.00 NIST
Inp 614.00 NIST
Inp 627.00 NIST
Inp 627.00 NIST
Inp 600.00 NIST
Inp 640.00 NIST
Inp 626.00 NIST
Inp 612.00 NIST
Inp 612.00 NIST
Inp Outlier 655.00 NIST
Inp Outlier 586.00 NIST
Inp 588.00 NIST
Inp Outlier 580.00 NIST
Inp 616.00 NIST
Inp 621.00 NIST
Inp 626.00 NIST
Inp 632.00 NIST
Inp 628.00 NIST
Inp 618.00 NIST
Inp 612.00 NIST
Inp 626.00 NIST
Inp 622.00 NIST
Inp 618.00 NIST
Inp 642.50 NIST
Inp 624.00 NIST
Inp 622.00 NIST
Inp 622.00 NIST
Inp 622.00 NIST
Inp 625.00 NIST
Inp 625.00 NIST
Inp 626.00 NIST
Inp 610.00 NIST
Inp 647.00 NIST
Inp 647.00 NIST
Inp 608.00 NIST
Inp 612.55 NIST
Inp 611.00 NIST
Inp 641.00 NIST
Inp 620.00 NIST
Inp 621.00 NIST
Inp Outlier 663.00 NIST
Inp 635.00 NIST
Inp 635.00 NIST
Inp 608.00 NIST
Inp 609.00 NIST
Inp 602.00 NIST
Inp 606.00 NIST
Inp 605.00 NIST
Inp 606.00 NIST
Inp 616.00 NIST
Inp 608.00 NIST
Inp 608.00 NIST
Inp 618.00 NIST
Inp 628.00 NIST
Inp 619.00 NIST
Inp Outlier 663.00 NIST
Inp 622.00 NIST
Inp Outlier 654.00 NIST
Inp 614.00 NIST
Inp 621.00 NIST
Inp 614.00 NIST
Inp 618.00 NIST
Inp 625.00 NIST
Inp 612.00 NIST
Inp 617.00 NIST
Inp 617.00 NIST
Inp 612.00 NIST
Inp 629.00 NIST
Inp 622.00 NIST
Inp 622.00 NIST
Inp 612.00 NIST
Inp 622.00 NIST
Inp 622.00 NIST
Inp 616.00 NIST
Inp 623.00 NIST
Inp 619.00 NIST
Inp 619.00 NIST
Inp 621.00 NIST
Inp 623.00 NIST
Inp 614.00 NIST
Inp 647.00 NIST
Inp 647.00 NIST
Inp 635.00 NIST
Inp 625.00 NIST
Inp 619.00 NIST
Inp 619.00 NIST
Inp 614.00 NIST
Inp 619.00 NIST
Inp 608.00 NIST
Inp 624.00 NIST
Inp 608.00 NIST
Inp 617.00 NIST
Inp 601.00 NIST
Inp 614.00 NIST
Inp 619.00 NIST
Inp 620.00 NIST
Inp 612.00 NIST
Inp Outlier 580.00 NIST
Inp 616.00 NIST
Inp 618.00 NIST
Inp 642.50 NIST
Inp 625.00 NIST
Inp 647.00 NIST
Inp 620.00 NIST
Inp 608.00 NIST
Inp 606.00 NIST
Inp 628.00 NIST
Inp 614.00 NIST
Inp 622.00 NIST
Inp 623.00 NIST
Inp 648.00 NIST
Ip [1043.00; 1129.00]   Show Hide
Ip 1108.00 NIST
Ip 1100.00 NIST
Ip 1094.00 NIST
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Ip 1100.00 NIST
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Ip 1122.00 NIST
Ip 1088.00 NIST
Ip 1090.00 NIST
Ip 1080.00 NIST
Ip 1092.00 NIST
Ip 1075.00 NIST
Ip 1083.00 NIST
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Ip 1087.00 NIST
Ip 1080.00 NIST
Ip 1101.00 NIST
Ip 1077.00 NIST
Ip 1091.00 NIST
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Ip 1092.00 NIST
Ip 1094.00 NIST
Ip 1094.00 NIST
Ip 1094.00 NIST
Ip 1110.00 NIST
Ip Outlier 1048.00 NIST
Ip 1114.00 NIST
Ip 1101.00 NIST
Ip Outlier 1053.00 NIST
Ip Outlier 1057.00 NIST
Ip 1060.00 NIST
Ip 1062.00 NIST
Ip 1085.00 NIST
Ip 1075.00 NIST
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Ip 1095.00 NIST
Ip 1086.00 NIST
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Ip 1094.00 NIST
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Ip 1098.00 NIST
Ip 1085.00 NIST
Ip 1090.00 NIST
Ip 1090.00 NIST
Ip 1112.00 NIST
Ip 1085.00 NIST
Ip Outlier 1056.00 NIST
Ip 1104.00 NIST
Ip 1097.00 NIST
Ip 1114.00 NIST
Ip Outlier 1043.00 NIST
Ip 1085.00 NIST
Ip 1093.00 NIST
Ip 1089.00 NIST
Ip 1078.00 NIST
Ip 1103.40 NIST
Ip 1065.00 NIST
Ip 1092.00 NIST
Ip 1064.00 NIST
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Ip 1103.00 NIST
Ip 1087.00 NIST
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Ip Outlier 1054.00 NIST
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Ip 1059.00 NIST
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Ip 1087.00 NIST
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Ip 1081.00 NIST
Ip Outlier 1125.00 NIST
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Ip 1122.00 NIST
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Ip 1086.00 NIST
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Ip 1105.00 NIST
Ip 1105.00 NIST
Ip 1110.00 NIST
Ip Outlier 1054.00 NIST
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Ip 1070.00 NIST
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Ip 1090.00 NIST
Ip 1100.00 NIST
Ip Outlier 1054.00 NIST
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Ip 1063.00 NIST
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Ip Outlier 1054.00 NIST
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Ip 1098.00 NIST
Ip 1096.00 NIST
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Ip 1119.00 NIST
Ip 1099.00 NIST
Ip 1099.00 NIST
Ip 1093.00 NIST
Ip Outlier 1054.00 NIST
Ip 1087.00 NIST
Ip 1113.00 NIST
Ip 1089.00 NIST
Ip 1108.00 NIST
Ip 1113.00 NIST
Ip 1113.00 NIST
Ip 1106.00 NIST
Ip 1108.00 NIST
Ip Outlier 1129.00 NIST
Ip 1097.00 NIST
Ip 1107.00 NIST
Ip 1108.00 NIST
Ip 1091.00 NIST
Ip 1108.00 NIST
Ip 1091.00 NIST
Ip 1086.00 NIST
Ip 1091.00 NIST
Ip 1072.00 NIST
Ip Outlier 1129.00 NIST
Ip 1093.00 NIST
Ip 1091.00 NIST
Ip 1096.00 NIST
Ip Outlier 1054.00 NIST
Ip 1091.00 NIST
Ip 1085.00 NIST
Ip 1084.00 NIST
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Ip 1089.00 NIST
Ip 1108.00 NIST
Ip 1091.00 NIST
Ip 1083.00 NIST
Ip 1091.00 NIST
Ip 1098.00 NIST
Ip 1094.00 NIST
Ip 1095.00 NIST
Ip 1095.00 NIST
Ip 1095.00 NIST
Ip 1114.00 NIST
Ip 1110.00 NIST
Ip 1110.00 NIST
Ip Outlier 1054.00 NIST
Ip 1090.00 NIST
Ip 1092.00 NIST
Ip 1084.00 NIST
Ip 1089.00 NIST
Ip 1122.00 NIST
Ip 1076.00 NIST
Ip 1108.00 NIST
Ip 1086.00 NIST
Ip 1093.00 NIST
Ip 1112.00 NIST
Ip 1114.00 NIST
Ip 1078.00 NIST
Ip 1092.00 NIST
Ip 1077.00 NIST
Ip 1121.00 NIST
Ip 1083.00 NIST
Ip 1068.00 NIST
Ip 1094.00 NIST
Ip 1080.00 NIST
Ip 1104.00 NIST
Ip 1059.00 NIST
Ip 1081.00 NIST
Ip 1087.00 NIST
Ip 1113.00 NIST
Ip 1110.00 NIST
Ip 1060.00 NIST
Ip 1062.00 NIST
Ip 1088.00 NIST
Ip 1100.00 NIST
Ip Outlier 1054.00 NIST
S°gas 350.00 J/mol×K NIST
S°liquid 214.50 J/mol×K NIST
S°solid,1 bar 140.70 J/mol×K NIST
Tboil [374.65; 410.55] K Show Hide
Tboil 381.05 K Measurement and correlation of binary vapor liquid equilibria of isomeric butanols with 1,4-dioxane
Tboil 380.15 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 380.83 K Isobaric Vapor Liquid Equilibrium for the Binary Systems of sec-Butyl Acetate + n-Butyl Alcohol, Isobutyl Alcohol, or tert-Butyl Alcohol at 101.3 kPa
Tboil 380.98 K Isobaric Vapor Liquid Equilibrium for the Binary and Ternary System with Isobutyl Alcohol, Isobutyl Acetate and Dimethyl Sulfoxide at 101.3 kPa
Tboil 380.93 K Vapor-Liquid Equilibrium of Binary Mixtures Containing Ethyl Acetate + 2-Methyl-1-propanol and Ethyl Acetate + 2-Methyl-1-butanol at 101.3 kPa
Tboil 381.00 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 380.92 K Vapor-Liquid Equilibrium Behaviors of Vanillin in 1-Butanol, 2-Butanol, and 2-Methyl-1-propanol
Tboil 380.92 K Vapor Liquid Equilibrium Behaviors of 5-Methyl-2-(1-methylethyl)phenol in Alcohol
Tboil 380.98 K High-Pressure Vapor-Liquid Equilibrium for Ethylene + 2-Methyl-1-propanol
Tboil 381.04 K ChemSep v8.3 pure component data Compiled value
Tboil 381.04 K KDB
Tboil 381.04 K NCMS SOLV-DB
Tboil 380.90 ± 0.40 K NIST
Tboil 381.30 K NIST
Tboil 380.97 ± 0.30 K NIST
Tboil 380.85 ± 0.30 K NIST
Tboil Outlier 410.55 ± 0.20 K NIST
Tboil 381.10 K NIST
Tboil 380.85 ± 0.40 K NIST
Tboil 380.85 ± 0.30 K NIST
Tboil 380.55 ± 0.20 K NIST
Tboil 381.25 ± 0.30 K NIST
Tboil 380.94 ± 0.40 K NIST
Tboil 381.10 ± 0.40 K NIST
Tboil 380.90 ± 0.40 K NIST
Tboil 380.90 ± 0.30 K NIST
Tboil 380.90 ± 0.30 K NIST
Tboil 381.05 ± 0.20 K NIST
Tboil 380.90 ± 0.10 K NIST
Tboil 381.95 ± 0.30 K NIST
Tboil 381.05 K NIST
Tboil 381.15 ± 0.40 K NIST
Tboil 381.03 ± 1.00 K NIST
Tboil 380.90 ± 0.10 K NIST
Tboil 379.15 ± 2.00 K NIST
Tboil 381.45 K NIST
Tboil 380.65 ± 1.00 K NIST
Tboil 379.15 ± 2.00 K NIST
Tboil 380.15 ± 1.00 K NIST
Tboil 381.15 ± 1.00 K NIST
Tboil 381.20 ± 0.38 K NIST
Tboil 379.90 ± 0.70 K NIST
Tboil 381.15 ± 1.00 K NIST
Tboil 381.15 ± 2.00 K NIST
Tboil 381.15 ± 1.00 K NIST
Tboil 378.65 ± 2.00 K NIST
Tboil 380.15 ± 2.00 K NIST
Tboil 379.65 ± 1.00 K NIST
Tboil 381.15 ± 0.50 K NIST
Tboil 381.05 ± 0.50 K NIST
Tboil 381.15 ± 0.50 K NIST
Tboil 381.20 ± 0.40 K NIST
Tboil 381.15 ± 0.50 K NIST
Tboil 381.80 ± 0.50 K NIST
Tboil 380.15 ± 1.00 K NIST
Tboil 381.00 ± 1.50 K NIST
Tboil 381.15 ± 0.50 K NIST
Tboil 380.15 ± 1.00 K NIST
Tboil 379.65 ± 1.00 K NIST
Tboil 380.00 ± 3.00 K NIST
Tboil 378.15 ± 5.00 K NIST
Tboil 381.15 ± 0.25 K NIST
Tboil 375.15 ± 5.00 K NIST
Tboil 380.65 ± 0.50 K NIST
Tboil 384.15 ± 3.00 K NIST
Tboil 380.35 ± 0.50 K NIST
Tboil 378.15 ± 2.00 K NIST
Tboil 374.65 ± 2.00 K NIST
Tboil 380.15 ± 1.00 K NIST
Tboil 380.65 ± 0.50 K NIST
Tboil 381.35 ± 0.50 K NIST
Tboil 380.75 ± 0.50 K NIST
Tboil 381.04 ± 0.10 K NIST
Tboil 380.65 ± 0.50 K NIST
Tboil 379.90 ± 1.50 K NIST
Tboil 380.55 ± 0.50 K NIST
Tboil 380.25 ± 0.50 K NIST
Tboil 380.96 ± 0.20 K NIST
Tboil 381.10 ± 0.30 K NIST
Tboil 381.15 ± 0.30 K NIST
Tboil 381.25 ± 0.15 K NIST
Tboil 381.00 ± 0.50 K NIST
Tboil 381.00 ± 0.50 K NIST
Tboil 381.00 ± 0.50 K NIST
Tboil 381.30 ± 0.20 K NIST
Tboil 381.00 ± 1.50 K NIST
Tboil 381.00 ± 0.50 K NIST
Tboil 381.20 ± 0.30 K NIST
Tboil 379.05 ± 1.00 K NIST
Tboil 380.85 ± 0.20 K NIST
Tboil 381.00 ± 0.30 K NIST
Tboil 380.15 ± 0.30 K NIST
Tboil 381.05 ± 0.50 K NIST
Tboil 380.62 ± 0.20 K NIST
Tboil 381.04 ± 0.10 K NIST
Tboil 380.40 ± 0.30 K NIST
Tboil 376.30 ± 0.20 K NIST
Tboil 378.20 ± 0.50 K NIST
Tboil 380.82 ± 0.30 K NIST
Tboil 380.79 ± 0.30 K NIST
Tboil 380.40 ± 0.50 K NIST
Tboil 379.55 ± 1.00 K NIST
Tc [538.20; 556.70] K Show Hide
Tc 547.80 K IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Tc 547.70 K PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc 547.78 K ChemSep v8.3 pure component data Compiled value
Tc 547.80 K KDB
Tc 547.80 ± 0.30 K NIST
Tc 548.60 K NIST
Tc 547.70 K NIST
Tc 547.78 ± 1.00 K NIST
Tc 547.74 K NIST
Tc Outlier 556.70 K NIST
Tc 547.77 K NIST
Tc 549.85 ± 0.30 K NIST
Tc 550.80 K NIST
Tc Outlier 538.20 K NIST
Tfus [165.00; 169.00] K Show Hide
Tfus 165.15 K Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus 165.15 K ChemSep v8.3 pure component data Compiled value
Tfus 165.00 K KDB
Tfus 165.15 K NCMS SOLV-DB
Tfus 165.15 ± 2.00 K NIST
Tfus 165.15 K NIST
Tfus Outlier 169.00 ± 2.00 K NIST
Ttriple [165.15; 171.20] K Show Hide
Ttriple 165.15 K ChemSep v8.3 pure component data Compiled value
Ttriple 171.18 K KDB
Ttriple 171.20 ± 0.01 K NIST
Ttriple 171.18 ± 0.02 K NIST
Ttriple 171.18 ± 0.02 K NIST
UQi 3.05 ChemSep v8.3 pure component data Compiled value
URi 3.45 ChemSep v8.3 pure component data Compiled value
Vc [0.273; 0.274] m3/kmol Show Hide
Vc 0.274 m3/kmol IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Vc 0.273 m3/kmol PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc 0.273 m3/kmol ChemSep v8.3 pure component data Compiled value
Vc 0.274 m3/kmol KDB
Vc 0.274 m3/kmol NIST
Zc [0.2580000; 0.2583780]   Show Hide
Zc 0.2580000 IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Zc 0.2580000 ChemSep v8.3 pure component data Compiled value
Zc 0.2583780 KDB
Zra 0.26 KDB

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,gas [133.74; 189.48] J/mol×K [379.99; 602.55] Show Hide
Cp,gas 133.74 J/mol×K 379.99 NIST
Cp,gas 134.34 J/mol×K 381.23 NIST
Cp,gas 140.10 ± 0.71 J/mol×K 390.55 NIST
Cp,gas 141.76 ± 0.71 J/mol×K 397.65 NIST
Cp,gas 139.55 J/mol×K 400.03 NIST
Cp,gas 143.92 ± 0.71 J/mol×K 406.95 NIST
Cp,gas 146.25 ± 0.71 J/mol×K 416.95 NIST
Cp,gas 147.91 ± 0.71 J/mol×K 424.05 NIST
Cp,gas 146.35 J/mol×K 425.01 NIST
Cp,gas 152.05 ± 0.71 J/mol×K 441.85 NIST
Cp,gas 152.97 J/mol×K 450.06 NIST
Cp,gas 154.24 ± 0.71 J/mol×K 451.25 NIST
Cp,gas 159.62 ± 0.71 J/mol×K 474.35 NIST
Cp,gas 158.94 J/mol×K 475.09 NIST
Cp,gas 160.41 ± 0.71 J/mol×K 477.75 NIST
Cp,gas 165.96 ± 0.71 J/mol×K 501.55 NIST
Cp,gas 171.62 ± 0.71 J/mol×K 525.85 NIST
Cp,gas 176.39 ± 0.71 J/mol×K 546.35 NIST
Cp,gas 184.92 ± 0.71 J/mol×K 582.95 NIST
Cp,gas 189.48 ± 0.71 J/mol×K 602.55 NIST
Cp,liquid [181.00; 215.10] J/mol×K [298.10; 333.00] Show Hide
Cp,liquid 184.10 J/mol×K 298.10 NIST
Cp,liquid 181.05 J/mol×K 298.15 NIST
Cp,liquid 182.01 J/mol×K 298.15 NIST
Cp,liquid 181.00 J/mol×K 298.15 NIST
Cp,liquid 185.40 J/mol×K 301.20 NIST
Cp,liquid 187.00 J/mol×K 303.00 NIST
Cp,liquid 185.60 J/mol×K 303.15 NIST
Cp,liquid 201.30 J/mol×K 323.00 NIST
Cp,liquid 215.10 J/mol×K 333.00 NIST
Cp,solid 129.20 J/mol×K 180.00 NIST
η [0.0008767; 0.0048050] Pa×s [288.15; 343.15] Show Hide
η 0.0048050 Pa×s 288.15 Densities and Viscosities of Binary Mixtures of 1-Bromobutane with Butanol Isomers at Several Temperatures
η 0.0048050 Pa×s 288.15 Densities and Viscosities of Binary Mixtures of 1-Chlorobutane with Butanol Isomers at Several Temperatures
η 0.0040366 Pa×s 293.15 Densities and Viscosities of Binary Liquid Mixtures of 2-Butanone with Branched Alcohols at (293.15 to 313.15) K
η 0.0039940 Pa×s 293.15 Viscosities and densities for binary mixtures of N-methylpiperazine with methanol, ethanol, n-propanol, iso-propanol, n-butanol and iso-butanol at 293.15, 298.15 and 303.15K
η 0.0040850 Pa×s 293.15 Experimental excess molar properties of binary mixtures of (3-amino-1-propanol + isobutanol, 2-propanol) at T = (293.15 to 333.15) K and modelling the excess molar volume by Prigogine-Flory-Patterson theory
η 0.0039430 Pa×s 293.15 Densities, Viscosities, and Excess Molar Enthalpies of 2-Pyrrolidone + Butanol Isomers at T ) (293.15, 298.15, and 303.15) K
η 0.0040855 Pa×s 293.15 Measurement and modeling the excess molar properties of binary mixtures of {[C6mim][BF4] + 3-amino-1-propanol} and {[C6mim][BF4] + isobutanol}: Application of Prigogine-Flory-Patterson theory
η 0.0034500 Pa×s 298.15 Measurement and modeling the excess molar properties of binary mixtures of {[C6mim][BF4] + 3-amino-1-propanol} and {[C6mim][BF4] + isobutanol}: Application of Prigogine-Flory-Patterson theory
η 0.0034040 Pa×s 298.15 Volumetric, transport, and acoustic properties of binary mixtures of 2-methyl-1-propanol with hexadecane and squalane at T = (298.15, 303.15, and 308.15) K: Experimental results, correlation, and prediction by the ERAS model
η 0.0034350 Pa×s 298.15 Densities and Viscosities of Binary Mixtures of 1-Bromobutane with Butanol Isomers at Several Temperatures
η 0.0033330 Pa×s 298.15 NCMS SOLV-DB
η 0.0033340 Pa×s 298.15 Viscosities and densities for binary mixtures of N-methylpiperazine with methanol, ethanol, n-propanol, iso-propanol, n-butanol and iso-butanol at 293.15, 298.15 and 303.15K
η 0.0033297 Pa×s 298.15 Densities and Viscosities of Binary Liquid Mixtures of 2-Butanone with Branched Alcohols at (293.15 to 313.15) K
η 0.0034350 Pa×s 298.15 Densities and Viscosities of Binary Mixtures of 1-Chlorobutane with Butanol Isomers at Several Temperatures
η 0.0033320 Pa×s 298.15 Densities, Viscosities, and Excess Molar Enthalpies of 2-Pyrrolidone + Butanol Isomers at T ) (293.15, 298.15, and 303.15) K
η 0.0028840 Pa×s 303.15 Densities, Viscosities, and Excess Molar Enthalpies of 2-Pyrrolidone + Butanol Isomers at T ) (293.15, 298.15, and 303.15) K
η 0.0026950 Pa×s 303.15 Volumetric, transport, and acoustic properties of binary mixtures of 2-methyl-1-propanol with hexadecane and squalane at T = (298.15, 303.15, and 308.15) K: Experimental results, correlation, and prediction by the ERAS model
η 0.0028770 Pa×s 303.15 Experimental excess molar properties of binary mixtures of (3-amino-1-propanol + isobutanol, 2-propanol) at T = (293.15 to 333.15) K and modelling the excess molar volume by Prigogine-Flory-Patterson theory
η 0.0028752 Pa×s 303.15 Densities and Viscosities of Binary Liquid Mixtures of 2-Butanone with Branched Alcohols at (293.15 to 313.15) K
η 0.0027940 Pa×s 303.15 Viscosities and densities for binary mixtures of N-methylpiperazine with methanol, ethanol, n-propanol, iso-propanol, n-butanol and iso-butanol at 293.15, 298.15 and 303.15K
η 0.0028767 Pa×s 303.15 Measurement and modeling the excess molar properties of binary mixtures of {[C6mim][BF4] + 3-amino-1-propanol} and {[C6mim][BF4] + isobutanol}: Application of Prigogine-Flory-Patterson theory
η 0.0026490 Pa×s 303.15 Densities and Viscosities of Binary Mixtures of n-Butanol with 2-Butanol, Isobutanol, and tert-Butanol from (303.15 to 343.15) K
η 0.0021880 Pa×s 308.15 Volumetric, transport, and acoustic properties of binary mixtures of 2-methyl-1-propanol with hexadecane and squalane at T = (298.15, 303.15, and 308.15) K: Experimental results, correlation, and prediction by the ERAS model
η 0.0024207 Pa×s 308.15 Densities and Viscosities of Binary Liquid Mixtures of 2-Butanone with Branched Alcohols at (293.15 to 313.15) K
η 0.0025080 Pa×s 308.15 Densities and Viscosities of Binary Mixtures of 1-Chlorobutane with Butanol Isomers at Several Temperatures
η 0.0022798 Pa×s 308.15 Densities and Viscosities of Binary Mixtures of n-Butanol with 2-Butanol, Isobutanol, and tert-Butanol from (303.15 to 343.15) K
η 0.0023845 Pa×s 308.15 Measurement and modeling the excess molar properties of binary mixtures of {[C6mim][BF4] + 3-amino-1-propanol} and {[C6mim][BF4] + isobutanol}: Application of Prigogine-Flory-Patterson theory
η 0.0025080 Pa×s 308.15 Densities and Viscosities of Binary Mixtures of 1-Bromobutane with Butanol Isomers at Several Temperatures
η 0.0019666 Pa×s 313.15 Densities and Viscosities of Binary Liquid Mixtures of 2-Butanone with Branched Alcohols at (293.15 to 313.15) K
η 0.0020909 Pa×s 313.15 Measurement and modeling the excess molar properties of binary mixtures of {[C6mim][BF4] + 3-amino-1-propanol} and {[C6mim][BF4] + isobutanol}: Application of Prigogine-Flory-Patterson theory
η 0.0020910 Pa×s 313.15 Experimental excess molar properties of binary mixtures of (3-amino-1-propanol + isobutanol, 2-propanol) at T = (293.15 to 333.15) K and modelling the excess molar volume by Prigogine-Flory-Patterson theory
η 0.0019653 Pa×s 313.15 Densities and Viscosities of Binary Mixtures of n-Butanol with 2-Butanol, Isobutanol, and tert-Butanol from (303.15 to 343.15) K
η 0.0018700 Pa×s 318.15 Densities and Viscosities of Binary Mixtures of 1-Bromobutane with Butanol Isomers at Several Temperatures
η 0.0018700 Pa×s 318.15 Densities and Viscosities of Binary Mixtures of 1-Chlorobutane with Butanol Isomers at Several Temperatures
η 0.0016921 Pa×s 318.15 Densities and Viscosities of Binary Mixtures of n-Butanol with 2-Butanol, Isobutanol, and tert-Butanol from (303.15 to 343.15) K
η 0.0018503 Pa×s 318.15 Measurement and modeling the excess molar properties of binary mixtures of {[C6mim][BF4] + 3-amino-1-propanol} and {[C6mim][BF4] + isobutanol}: Application of Prigogine-Flory-Patterson theory
η 0.0015759 Pa×s 323.15 Measurement and modeling the excess molar properties of binary mixtures of {[C6mim][BF4] + 3-amino-1-propanol} and {[C6mim][BF4] + isobutanol}: Application of Prigogine-Flory-Patterson theory
η 0.0015760 Pa×s 323.15 Experimental excess molar properties of binary mixtures of (3-amino-1-propanol + isobutanol, 2-propanol) at T = (293.15 to 333.15) K and modelling the excess molar volume by Prigogine-Flory-Patterson theory
η 0.0014825 Pa×s 323.15 Densities and Viscosities of Binary Mixtures of n-Butanol with 2-Butanol, Isobutanol, and tert-Butanol from (303.15 to 343.15) K
η 0.0012967 Pa×s 328.15 Measurement and modeling the excess molar properties of binary mixtures of {[C6mim][BF4] + 3-amino-1-propanol} and {[C6mim][BF4] + isobutanol}: Application of Prigogine-Flory-Patterson theory
η 0.0012675 Pa×s 328.15 Densities and Viscosities of Binary Mixtures of n-Butanol with 2-Butanol, Isobutanol, and tert-Butanol from (303.15 to 343.15) K
η 0.0011243 Pa×s 333.15 Measurement and modeling the excess molar properties of binary mixtures of {[C6mim][BF4] + 3-amino-1-propanol} and {[C6mim][BF4] + isobutanol}: Application of Prigogine-Flory-Patterson theory
η 0.0011163 Pa×s 333.15 Densities and Viscosities of Binary Mixtures of n-Butanol with 2-Butanol, Isobutanol, and tert-Butanol from (303.15 to 343.15) K
η 0.0011240 Pa×s 333.15 Experimental excess molar properties of binary mixtures of (3-amino-1-propanol + isobutanol, 2-propanol) at T = (293.15 to 333.15) K and modelling the excess molar volume by Prigogine-Flory-Patterson theory
η 0.0009876 Pa×s 338.15 Measurement and modeling the excess molar properties of binary mixtures of {[C6mim][BF4] + 3-amino-1-propanol} and {[C6mim][BF4] + isobutanol}: Application of Prigogine-Flory-Patterson theory
η 0.0009851 Pa×s 338.15 Densities and Viscosities of Binary Mixtures of n-Butanol with 2-Butanol, Isobutanol, and tert-Butanol from (303.15 to 343.15) K
η 0.0008767 Pa×s 343.15 Densities and Viscosities of Binary Mixtures of n-Butanol with 2-Butanol, Isobutanol, and tert-Butanol from (303.15 to 343.15) K
εr [16.53; 19.51]   [288.15; 308.15] Show Hide
εr 19.51 288.15 Static Permittivities of Isomeric Butanol Mixtures at Temperatures from (288.15 to 308.15) K
εr 18.71 293.15 Static Permittivities of Isomeric Butanol Mixtures at Temperatures from (288.15 to 308.15) K
εr 17.96 298.15 Static Permittivities of Isomeric Butanol Mixtures at Temperatures from (288.15 to 308.15) K
εr 17.23 303.15 Static Permittivities of Isomeric Butanol Mixtures at Temperatures from (288.15 to 308.15) K
εr 16.53 308.15 Static Permittivities of Isomeric Butanol Mixtures at Temperatures from (288.15 to 308.15) K
ΔfusH [6.32; 6.32] kJ/mol [171.18; 171.20] Show Hide
ΔfusH 6.32 kJ/mol 171.18 NIST
ΔfusH 6.32 kJ/mol 171.18 NIST
ΔfusH 6.32 kJ/mol 171.20 NIST
ΔfusH 6.32 kJ/mol 171.20 NIST
ΔfusH 6.32 kJ/mol 171.20 NIST
ΔfusH 6.32 kJ/mol 171.20 NIST
ΔvapH [36.20; 55.00] kJ/mol [106.90; 515.50] Show Hide
ΔvapH 50.71 kJ/mol 106.90 NIST
ΔvapH 55.00 kJ/mol 222.50 NIST
ΔvapH 49.70 ± 0.10 kJ/mol 313.00 NIST
ΔvapH 48.30 ± 0.10 kJ/mol 328.00 NIST
ΔvapH 52.60 kJ/mol 340.50 NIST
ΔvapH 46.20 ± 0.10 kJ/mol 347.00 NIST
ΔvapH 48.10 kJ/mol 351.00 NIST
ΔvapH 47.00 kJ/mol 357.00 NIST
ΔvapH 45.00 ± 0.10 kJ/mol 358.00 NIST
ΔvapH 49.50 kJ/mol 362.00 NIST
ΔvapH 44.20 ± 0.10 kJ/mol 363.00 NIST
ΔvapH 46.20 kJ/mol 365.50 NIST
ΔvapH 45.20 kJ/mol 370.50 NIST
ΔvapH 45.40 kJ/mol 375.00 NIST
ΔvapH 44.20 kJ/mol 379.00 NIST
ΔvapH 41.90 ± 0.10 kJ/mol 381.00 NIST
ΔvapH 41.82 kJ/mol 381.10 NIST
ΔvapH 42.60 kJ/mol 399.50 NIST
ΔvapH 41.10 kJ/mol 447.00 NIST
ΔvapH 46.00 kJ/mol 452.50 NIST
ΔvapH 40.10 kJ/mol 485.50 NIST
ΔvapH 36.20 kJ/mol 515.50 NIST
ν [0.0000027; 0.0000042] m2/s [298.15; 313.15] Show Hide
ν 0.0000042 m2/s 298.15 Viscosities of Binary Mixtures of Isomeric Butanols or Isomeric Chlorobutanes with 2-Methyltetrahydrofuran
ν 0.0000027 m2/s 313.15 Viscosities of Binary Mixtures of Isomeric Butanols or Isomeric Chlorobutanes with 2-Methyltetrahydrofuran
Pvap [0.34; 2505.00] kPa [278.15; 513.15] Show Hide
Pvap 0.34 kPa 278.15 Vapor Liquid Equilibrium between (278.15 and 323.15) K and Excess Functions at T = 298.15 K for 1-Bromobutane with 2-Methyl-1-propanol or 2-Butanol
Pvap 0.51 kPa 283.15 Vapor Liquid Equilibrium between (278.15 and 323.15) K and Excess Functions at T = 298.15 K for 1-Bromobutane with 2-Methyl-1-propanol or 2-Butanol
Pvap 0.74 kPa 288.15 Vapor Liquid Equilibrium between (278.15 and 323.15) K and Excess Functions at T = 298.15 K for 1-Bromobutane with 2-Methyl-1-propanol or 2-Butanol
Pvap 1.06 kPa 293.15 Vapor Liquid Equilibrium between (278.15 and 323.15) K and Excess Functions at T = 298.15 K for 1-Bromobutane with 2-Methyl-1-propanol or 2-Butanol
Pvap 1.39 kPa 298.15 NCMS SOLV-DB
Pvap 1.50 kPa 298.15 Vapor Liquid Equilibrium between (278.15 and 323.15) K and Excess Functions at T = 298.15 K for 1-Bromobutane with 2-Methyl-1-propanol or 2-Butanol
Pvap 2.13 kPa 303.15 Vapor Liquid Equilibrium between (278.15 and 323.15) K and Excess Functions at T = 298.15 K for 1-Bromobutane with 2-Methyl-1-propanol or 2-Butanol
Pvap 2.96 kPa 308.15 Vapor Liquid Equilibrium between (278.15 and 323.15) K and Excess Functions at T = 298.15 K for 1-Bromobutane with 2-Methyl-1-propanol or 2-Butanol
Pvap 4.03 kPa 313.15 Vapor Liquid Equilibrium between (278.15 and 323.15) K and Excess Functions at T = 298.15 K for 1-Bromobutane with 2-Methyl-1-propanol or 2-Butanol
Pvap 5.44 kPa 318.15 Vapor Liquid Equilibrium between (278.15 and 323.15) K and Excess Functions at T = 298.15 K for 1-Bromobutane with 2-Methyl-1-propanol or 2-Butanol
Pvap 7.24 kPa 323.15 Vapor Liquid Equilibrium between (278.15 and 323.15) K and Excess Functions at T = 298.15 K for 1-Bromobutane with 2-Methyl-1-propanol or 2-Butanol
Pvap 15.00 kPa 336.90 Complementary vapor pressure data for 2-methyl-1-propanol and 3-methyl-1-butanol at a pressure range of (15 to 177) kPa
Pvap 30.00 kPa 351.20 Complementary vapor pressure data for 2-methyl-1-propanol and 3-methyl-1-butanol at a pressure range of (15 to 177) kPa
Pvap 40.00 kPa 357.45 Isobaric Vapor-Liquid Equilibria for Tetrahydropyran and Alcohol Systems
Pvap 40.00 kPa 357.70 Complementary vapor pressure data for 2-methyl-1-propanol and 3-methyl-1-butanol at a pressure range of (15 to 177) kPa
Pvap 50.00 kPa 362.90 Complementary vapor pressure data for 2-methyl-1-propanol and 3-methyl-1-butanol at a pressure range of (15 to 177) kPa
Pvap 53.33 kPa 364.17 Isobaric Vapor-Liquid Equilibria for Tetrahydropyran and Alcohol Systems
Pvap 60.00 kPa 367.40 Complementary vapor pressure data for 2-methyl-1-propanol and 3-methyl-1-butanol at a pressure range of (15 to 177) kPa
Pvap 66.66 kPa 369.67 Isobaric Vapor-Liquid Equilibria for Tetrahydropyran and Alcohol Systems
Pvap 70.00 kPa 371.30 Complementary vapor pressure data for 2-methyl-1-propanol and 3-methyl-1-butanol at a pressure range of (15 to 177) kPa
Pvap 79.99 kPa 374.35 Isobaric Vapor-Liquid Equilibria for Tetrahydropyran and Alcohol Systems
Pvap 80.00 kPa 374.70 Complementary vapor pressure data for 2-methyl-1-propanol and 3-methyl-1-butanol at a pressure range of (15 to 177) kPa
Pvap 90.00 kPa 377.80 Complementary vapor pressure data for 2-methyl-1-propanol and 3-methyl-1-butanol at a pressure range of (15 to 177) kPa
Pvap 93.32 kPa 378.45 Isobaric Vapor-Liquid Equilibria for Tetrahydropyran and Alcohol Systems
Pvap 98.66 kPa 379.96 Isobaric Vapor-Liquid Equilibria for Tetrahydropyran and Alcohol Systems
Pvap 100.00 kPa 380.70 Complementary vapor pressure data for 2-methyl-1-propanol and 3-methyl-1-butanol at a pressure range of (15 to 177) kPa
Pvap 110.00 kPa 383.30 Complementary vapor pressure data for 2-methyl-1-propanol and 3-methyl-1-butanol at a pressure range of (15 to 177) kPa
Pvap 120.00 kPa 385.80 Complementary vapor pressure data for 2-methyl-1-propanol and 3-methyl-1-butanol at a pressure range of (15 to 177) kPa
Pvap 130.00 kPa 388.00 Complementary vapor pressure data for 2-methyl-1-propanol and 3-methyl-1-butanol at a pressure range of (15 to 177) kPa
Pvap 140.00 kPa 390.20 Complementary vapor pressure data for 2-methyl-1-propanol and 3-methyl-1-butanol at a pressure range of (15 to 177) kPa
Pvap 150.00 kPa 392.20 Complementary vapor pressure data for 2-methyl-1-propanol and 3-methyl-1-butanol at a pressure range of (15 to 177) kPa
Pvap 1113.00 kPa 468.15 Vapor-Liquid Equilibria for the n-Pentane + 1-Propanol and n-Pentane + 2-Methyl-1-propanol Systems near the Critical Region
Pvap 1506.00 kPa 483.15 Vapor-Liquid Equilibria for the n-Pentane + 1-Propanol and n-Pentane + 2-Methyl-1-propanol Systems near the Critical Region
Pvap 1933.00 kPa 498.15 Vapor-Liquid Equilibria for the n-Pentane + 1-Propanol and n-Pentane + 2-Methyl-1-propanol Systems near the Critical Region
Pvap 2505.00 kPa 513.15 Vapor-Liquid Equilibria for the n-Pentane + 1-Propanol and n-Pentane + 2-Methyl-1-propanol Systems near the Critical Region
n0 [1.38390; 1.39620]   [293.15; 308.15] Show Hide
n0 1.39620 293.15 Excess Properties and Phase Equilibria for the Potential Biofuel System of Propan-2-ol and 2-Methyl-propan-1-ol at 333.15, 343.15, and 353.15 K
n0 1.39563 293.15 Ternary Liquid Liquid Equilibrium Data for the Water + Acetonitrile + {Butan-1-ol or 2-Methylpropan-1-ol} Systems at (303.2, 323.2, 343.2) K and 1 atm
n0 1.39540 293.15 Vapor Liquid Equilibrium Data for Binary Systems of n-Dodecane + {Propan-1-ol, Butan-1-ol, 2-Methylpropan-1-ol} at 40 kPa
n0 1.39550 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 1.39290 293.15 Volumetric Properties of Highly Nonideal Binary Mixtures Containing Ethanoic Acid and Propanoic Acid with Butan-2-ol, Methyl-2-propanol, and 2-Methyl-2-butanol at Different Temperatures
n0 1.39570 293.15 Solid-Liquid Equilibrium Measurements for Posaconazole and Voriconazole in Several Solvents between T = 278.2 and 323.2 K Using Differential Thermal Analysis/Thermal Gravimetric Analysis
n0 1.39580 293.15 Isothermal Vapor-Liquid Equilibrium Measurements for Alcohol + Water/n-Hexane Azeotropic Systems Using Both Dynamic and Automated Static-Synthetic Methods
n0 1.39570 293.15 Isothermal Vapor-Liquid Equilibrium Measurements of Butan-2-one + 2-Methyl-propan-1-ol/Pentan-1-ol
n0 1.39590 293.15 Isothermal Vapor-Liquid Equilibrium for the 2-Pentanone (MPK) + 2-Methyl Propan-1-ol Binary Mixture
n0 1.39580 293.15 Vapour-liquid equilibrium of carboxylic acid alcohol binary systems:2-Propanol + butyric acid, 2-butanol + butyric acid and 2-methyl-1-propanol + butyric acid
n0 1.39550 293.15 Liquid-liquid equilibrium for the ternary system water + 2-methyl-1-propanol + butyl acetate and water + 2-methyl-2-propanol + butyl acetate at (298.15 and 323.15) K
n0 1.39260 295.15 Isobaric Vapor Liquid Equilibrium Data for Binary Mixtures of 1-Phenylethanone with a Few Alcohols at 95.2 kPa
n0 1.39390 298.15 Excess Gibbs free energies of the binary mixtures of acetonitrile with butanols at 94.83 kPa
n0 1.38390 298.15 Bubble Temperatures of the Binary Mixtures of Dimethylcarbonate with Some Alcohols at 95.8 kPa
n0 1.39400 298.15 NCMS SOLV-DB
n0 1.39390 298.15 (Vapor + liquid) equilibria of the binary mixtures of m-cresol with C1 C4 aliphatic alcohols at 95.5 kPa
n0 1.39370 298.15 Isobaric vapor-liquid equilibria for the binary systems isobutyl alcohol + isobutyl acetate and tert-butyl alcohol + tert-butyl acetate at 20 and 101.3 kPa
n0 1.39390 298.15 Isobaric (vapour + liquid) equilibrium for N-methyl-2-pyrrolidone with branched alcohols
n0 1.39320 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 1.39380 298.15 Volumetric behavior of carbon dioxide + 2-methyl-1-propanol and carbondioxide + 2-methyl-2-propanol mixtures at 313.15 K
n0 1.39380 298.15 Study of liquid liquid equilibrium of the systems isobutyl acetate + acetic acid +water and isobutyl alcohol + acetic acid +water at different temperatures
n0 1.39380 298.15 Liquid liquid equilibria of the systems isobutyl acetate + isobutyl alcohol +water and isobutyl acetate + isobutyl alcohol + glycerol at different temperatures
n0 1.39390 298.15 Excess volumes and excess enthalpies of N-methyl-2-pyrrolidone with branched alcohols
n0 1.39380 298.15 Dielectric Properties of Methanol Mixtures with Ethanol, Isomers of Propanol, and Butanol
n0 1.39390 298.15 Bubble-Temperature Measurements on Some Binary Mixtures Formed by Tetrahydrofuran or Amyl Alcohol with Hydrocarbons, Chlorohydrocarbons, or Butanols at (94.6 or 95.8) kPa
n0 1.39370 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 1.39390 298.15 Excess Gibbs energies of selected binary mixtures formed by N,N-dimethyl formamide at 95.5 kPa
n0 1.39390 298.15 Activity coefficients of the binary mixtures of a-cresol or p-cresol with C l-C4 aliphatic alcohols near ambient pressure
n0 1.39380 298.15 Vapor liquid equilibria in the ternary system isobutyl alcohol + isobutyl acetate + butyl propionate and the binary systems isobutyl alcohol + butyl propionate, isobutyl acetate + butyl propionate at 101.3 kPa
n0 1.39370 298.15 Phase equilibria in the ternary system isobutyl alcohol + isobutyl acetate + 1-hexanol and the binary systems isobutyl alcohol + 1-hexanol, isobutyl acetate + 1-hexanol at 101.3 kPa
n0 1.39370 298.15 Phase equilibria in the systems isobutyl alcohol +N,N-dimethylformamide, isobutyl acetate +N,N-dimethylformamide and isobutyl alcohol + isobutyl acetate +N,N-dimethylformamide at 101.3 kPa
n0 1.39170 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 1.38960 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
ρl [756.43; 806.12] kg/m3 [288.15; 348.15] Show Hide
ρl 805.60 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 805.88 kg/m3 288.15 Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl 806.12 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 802.00 kg/m3 293.00 KDB
ρl 802.03 kg/m3 293.15 Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl 801.80 kg/m3 293.15 Measurement and correlation of isobaric vapour-liquid equilibria for binary systems of 1-(methoxymethoxy)-2-methyl-propane with 1-butanol and isobutanol at 101.33 kPa
ρl 801.98 kg/m3 293.15 Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Butanol, + Isobutyl Alcohol, or + 2-Butanol from 293.15 to 333.15 K at 0.1 MPa
ρl 801.80 kg/m3 293.15 Measurement and Correlation of Isobaric Vapor Liquid Equilibrium for Binary Systems of 1-(Ethoxymethoxy)-2-methyl-propane with Isobutyl Alcohol or 1-Butanol at 101.33 kPa
ρl 801.98 kg/m3 293.15 Density, Speed of Sound, Viscosity, Excess Properties, and Prigogine Flory Patterson (PFP) Theory of Binary Mixtures of Amine and Alcohols
ρl 801.82 kg/m3 293.15 Density and Viscosity Measurements of Binary Alkanol Mixtures from (293.15 to 333.15) K at Atmospheric Pressure
ρl 801.96 kg/m3 293.15 Experimental and Computational Studies of Binary Mixtures of Isobutanol + Cyclohexylamine
ρl 801.48 kg/m3 293.15 Densities and Volumetric Properties of Binary Mixtures of Aniline with 1-Propanol, 2-Propanol, 2-Methyl-1-Propanol, and 2-Methyl-2-Propanol at Temperatures from 293.15 to 318.15 K
ρl 801.70 kg/m3 293.15 Measurement and correlation of liquid liquid equilibrium data for 2-methyl-1-propanol + 2-propanol + water at several temperatures
ρl 801.85 kg/m3 293.15 Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
ρl 797.84 kg/m3 298.15 Volumetric properties for binary and ternary systems consist of 1-chlorobutane, n-butylamine and isobutanol at 298.15 K with application of the Prigogine-Flory-Patterson theory and ERAS-Model
ρl 797.92 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 797.98 kg/m3 298.15 (Vapour + liquid) equilibrium of binary mixtures (1,3-dioxolane or 1,4-dioxane + 2-methyl-1-propanol or 2-methyl-2-propanol) at isobaric conditions
ρl 797.99 kg/m3 298.15 Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
ρl 798.13 kg/m3 298.15 Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Butanol, + Isobutyl Alcohol, or + 2-Butanol from 293.15 to 333.15 K at 0.1 MPa
ρl 797.83 kg/m3 298.15 Proposal for a Viscous Test Mixture Densities, Viscosities, and Vapor Liquid Equilibrium Data of the Binary Mixture 2-Methyl-2-butanol + 2-Methyl-1-propanol
ρl 801.65 kg/m3 298.15 Liquid-Liquid Equilibrium for Ternary Systems, Water + 5-Hydroxymethylfurfural + (1-Butanol, Isobutanol, Methyl Isobutyl Ketone), at 313.15, 323.15, and 333.15 K
ρl 797.83 kg/m3 298.15 Excess Molar Volumes and Surface Tensions of 1,2,4-Trimethylbenzene and 1,3,5-Trimethylbenzene with 1-Butanol, 2-Methyl-1-propanol, 2-Butanol, and 2-Methyl-2-propanol at 298.15 K
ρl 798.12 kg/m3 298.15 Experimental and Computational Studies of Binary Mixtures of Isobutanol + Cyclohexylamine
ρl 797.54 kg/m3 298.15 Densities and Volumetric Properties of Binary Mixtures of Aniline with 1-Propanol, 2-Propanol, 2-Methyl-1-Propanol, and 2-Methyl-2-Propanol at Temperatures from 293.15 to 318.15 K
ρl 797.82 kg/m3 298.15 Experimental and theoretical excess molar properties of imidazolium based ionic liquids with isomers of butanol
ρl 797.77 kg/m3 298.15 Densities and Viscosities of the Ternary Mixtures 2-Methyl-1-propanol (or 2-Methyl-2-propanol) + N-Hexane + 1-Chlorobutane at 298.15 K
ρl 798.16 kg/m3 298.15 Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl 797.80 kg/m3 298.15 Bubble point temperatures of the binary mixtures of nitrobenzene with C1 C4 aliphatic alcohols at 94.95 kPa
ρl 798.10 kg/m3 298.15 Density, Speed of Sound, Viscosity, Excess Properties, and Prigogine Flory Patterson (PFP) Theory of Binary Mixtures of Amine and Alcohols
ρl 798.10 kg/m3 298.15 Densities, Viscosities, and Speeds of Sound of Binary Liquid Mixtures of Ethylenediamine with Alcohols at T = (293.15 to 313.15) K
ρl 798.41 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 797.77 kg/m3 298.15 Surface Tensions of the Ternary Mixtures Containing an Isomeric Butanol + n-Hexane + 1-Chlorobutane at 298.15 K
ρl 798.32 kg/m3 298.15 Densities and Viscosities for Binary Liquid Mixtures of Butan-1-ol + Propane-1,2-diol, + Butane-1,2-diol and 2-Methylpropan-1-ol + Propane-1,2-diol, + Butane-1,2-diol from 298.15 to 333.15 K at 0.1 MPa
ρl 795.35 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 794.25 kg/m3 303.15 Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl 794.22 kg/m3 303.15 Experimental and Computational Studies of Binary Mixtures of Isobutanol + Cyclohexylamine
ρl 793.60 kg/m3 303.15 Densities and Volumetric Properties of Binary Mixtures of Aniline with 1-Propanol, 2-Propanol, 2-Methyl-1-Propanol, and 2-Methyl-2-Propanol at Temperatures from 293.15 to 318.15 K
ρl 794.43 kg/m3 303.15 Densities and Viscosities for Binary Liquid Mixtures of Butan-1-ol + Propane-1,2-diol, + Butane-1,2-diol and 2-Methylpropan-1-ol + Propane-1,2-diol, + Butane-1,2-diol from 298.15 to 333.15 K at 0.1 MPa
ρl 794.06 kg/m3 303.15 Density and Viscosity Measurements of Binary Alkanol Mixtures from (293.15 to 333.15) K at Atmospheric Pressure
ρl 794.20 kg/m3 303.15 Density, Speed of Sound, Viscosity, Excess Properties, and Prigogine Flory Patterson (PFP) Theory of Binary Mixtures of Amine and Alcohols
ρl 794.03 kg/m3 303.15 Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
ρl 794.24 kg/m3 303.15 Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Butanol, + Isobutyl Alcohol, or + 2-Butanol from 293.15 to 333.15 K at 0.1 MPa
ρl 790.09 kg/m3 308.15 Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
ρl 790.12 kg/m3 308.15 Densities and Viscosities of Binary Mixtures of 2-Butanol + Isobutanol, 2-Butanol + tert-Butanol, and Isobutanol + tert-Butanol from (308.15 to 343.15) K
ρl 789.66 kg/m3 308.15 Densities and Volumetric Properties of Binary Mixtures of Aniline with 1-Propanol, 2-Propanol, 2-Methyl-1-Propanol, and 2-Methyl-2-Propanol at Temperatures from 293.15 to 318.15 K
ρl 790.27 kg/m3 308.15 Experimental and Computational Studies of Binary Mixtures of Isobutanol + Cyclohexylamine
ρl 790.29 kg/m3 308.15 Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Butanol, + Isobutyl Alcohol, or + 2-Butanol from 293.15 to 333.15 K at 0.1 MPa
ρl 790.31 kg/m3 308.15 Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl 790.63 kg/m3 308.15 Experimental and theoretical excess molar properties of imidazolium based ionic liquids with isomers of butanol
ρl 790.25 kg/m3 308.15 Density, Speed of Sound, Viscosity, Excess Properties, and Prigogine Flory Patterson (PFP) Theory of Binary Mixtures of Amine and Alcohols
ρl 790.49 kg/m3 308.15 Densities and Viscosities for Binary Liquid Mixtures of Butan-1-ol + Propane-1,2-diol, + Butane-1,2-diol and 2-Methylpropan-1-ol + Propane-1,2-diol, + Butane-1,2-diol from 298.15 to 333.15 K at 0.1 MPa
ρl 786.12 kg/m3 313.15 Densities and Viscosities of Binary Mixtures of 2-Butanol + Isobutanol, 2-Butanol + tert-Butanol, and Isobutanol + tert-Butanol from (308.15 to 343.15) K
ρl 786.48 kg/m3 313.15 Densities and Viscosities for Binary Liquid Mixtures of Butan-1-ol + Propane-1,2-diol, + Butane-1,2-diol and 2-Methylpropan-1-ol + Propane-1,2-diol, + Butane-1,2-diol from 298.15 to 333.15 K at 0.1 MPa
ρl 786.12 kg/m3 313.15 Density and Viscosity Measurements of Binary Alkanol Mixtures from (293.15 to 333.15) K at Atmospheric Pressure
ρl 786.24 kg/m3 313.15 Density, Speed of Sound, Viscosity, Excess Properties, and Prigogine Flory Patterson (PFP) Theory of Binary Mixtures of Amine and Alcohols
ρl 785.72 kg/m3 313.15 Densities and Volumetric Properties of Binary Mixtures of Aniline with 1-Propanol, 2-Propanol, 2-Methyl-1-Propanol, and 2-Methyl-2-Propanol at Temperatures from 293.15 to 318.15 K
ρl 786.12 kg/m3 313.15 Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
ρl 786.30 kg/m3 313.15 Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Butanol, + Isobutyl Alcohol, or + 2-Butanol from 293.15 to 333.15 K at 0.1 MPa
ρl 786.31 kg/m3 313.15 Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl 786.51 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 786.07 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 786.27 kg/m3 313.15 Experimental and Computational Studies of Binary Mixtures of Isobutanol + Cyclohexylamine
ρl 781.97 kg/m3 318.15 Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
ρl 782.42 kg/m3 318.15 Densities and Viscosities for Binary Liquid Mixtures of Butan-1-ol + Propane-1,2-diol, + Butane-1,2-diol and 2-Methylpropan-1-ol + Propane-1,2-diol, + Butane-1,2-diol from 298.15 to 333.15 K at 0.1 MPa
ρl 781.78 kg/m3 318.15 Densities and Volumetric Properties of Binary Mixtures of Aniline with 1-Propanol, 2-Propanol, 2-Methyl-1-Propanol, and 2-Methyl-2-Propanol at Temperatures from 293.15 to 318.15 K
ρl 782.26 kg/m3 318.15 Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl 781.98 kg/m3 318.15 Experimental and theoretical excess molar properties of imidazolium based ionic liquids with isomers of butanol
ρl 782.24 kg/m3 318.15 Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Butanol, + Isobutyl Alcohol, or + 2-Butanol from 293.15 to 333.15 K at 0.1 MPa
ρl 782.06 kg/m3 318.15 Densities and Viscosities of Binary Mixtures of 2-Butanol + Isobutanol, 2-Butanol + tert-Butanol, and Isobutanol + tert-Butanol from (308.15 to 343.15) K
ρl 777.86 kg/m3 323.15 Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
ρl 778.30 kg/m3 323.15 Densities and Viscosities for Binary Liquid Mixtures of Butan-1-ol + Propane-1,2-diol, + Butane-1,2-diol and 2-Methylpropan-1-ol + Propane-1,2-diol, + Butane-1,2-diol from 298.15 to 333.15 K at 0.1 MPa
ρl 777.93 kg/m3 323.15 Densities and Viscosities of Binary Mixtures of 2-Butanol + Isobutanol, 2-Butanol + tert-Butanol, and Isobutanol + tert-Butanol from (308.15 to 343.15) K
ρl 778.14 kg/m3 323.15 Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl 778.12 kg/m3 323.15 Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Butanol, + Isobutyl Alcohol, or + 2-Butanol from 293.15 to 333.15 K at 0.1 MPa
ρl 777.94 kg/m3 323.15 Density and Viscosity Measurements of Binary Alkanol Mixtures from (293.15 to 333.15) K at Atmospheric Pressure
ρl 774.11 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 773.73 kg/m3 328.15 Densities and Viscosities of Binary Mixtures of 2-Butanol + Isobutanol, 2-Butanol + tert-Butanol, and Isobutanol + tert-Butanol from (308.15 to 343.15) K
ρl 774.09 kg/m3 328.15 Densities and Viscosities for Binary Liquid Mixtures of Butan-1-ol + Propane-1,2-diol, + Butane-1,2-diol and 2-Methylpropan-1-ol + Propane-1,2-diol, + Butane-1,2-diol from 298.15 to 333.15 K at 0.1 MPa
ρl 773.69 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 773.92 kg/m3 328.15 Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Butanol, + Isobutyl Alcohol, or + 2-Butanol from 293.15 to 333.15 K at 0.1 MPa
ρl 769.44 kg/m3 333.15 Densities and Viscosities of Binary Mixtures of 2-Butanol + Isobutanol, 2-Butanol + tert-Butanol, and Isobutanol + tert-Butanol from (308.15 to 343.15) K
ρl 769.65 kg/m3 333.15 Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Butanol, + Isobutyl Alcohol, or + 2-Butanol from 293.15 to 333.15 K at 0.1 MPa
ρl 769.46 kg/m3 333.15 Density and Viscosity Measurements of Binary Alkanol Mixtures from (293.15 to 333.15) K at Atmospheric Pressure
ρl 769.81 kg/m3 333.15 Densities and Viscosities for Binary Liquid Mixtures of Butan-1-ol + Propane-1,2-diol, + Butane-1,2-diol and 2-Methylpropan-1-ol + Propane-1,2-diol, + Butane-1,2-diol from 298.15 to 333.15 K at 0.1 MPa
ρl 765.45 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 765.07 kg/m3 338.15 Densities and Viscosities of Binary Mixtures of 2-Butanol + Isobutanol, 2-Butanol + tert-Butanol, and Isobutanol + tert-Butanol from (308.15 to 343.15) K
ρl 760.61 kg/m3 343.15 Densities and Viscosities of Binary Mixtures of 2-Butanol + Isobutanol, 2-Butanol + tert-Butanol, and Isobutanol + tert-Butanol from (308.15 to 343.15) K
ρl 756.43 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
ΔfusS [36.93; 36.93] J/mol×K [171.18; 171.18] Show Hide
ΔfusS 36.93 J/mol×K 171.18 NIST
ΔfusS 36.93 J/mol×K 171.18 NIST
csound,fluid [1108.20; 1238.70] m/s [283.15; 323.15] Show Hide
csound,fluid 1238.70 m/s 283.15 Excess Enthalpy, Density, and Speed of Sound for the Mixtures a-Pinene + 2-Methyl-1-propanol or 2-Methyl-2-propanol at Several Temperatures
csound,fluid 1204.10 m/s 293.15 Acoustic and Thermophysical Properties of Binary Liquid Mixtures of Primary Butanols with Hexane and Cyclohexane at 293.15 K
csound,fluid 1188.50 m/s 298.15 Densities and speeds of sound for binary mixtures of (1,3-dioxolane or 1,4-dioxane) with (2-methyl-1-propanol or 2-methyl-2-propanol) at the temperatures 298.15 K and 313.15 K
csound,fluid 1188.00 m/s 298.15 Excess Enthalpy, Density, and Speed of Sound for the Mixtures a-Pinene + 2-Methyl-1-propanol or 2-Methyl-2-propanol at Several Temperatures
csound,fluid 1174.30 m/s 303.15 Excess Enthalpy, Density, and Speed of Sound for the Mixtures a-Pinene + 2-Methyl-1-propanol or 2-Methyl-2-propanol at Several Temperatures
csound,fluid 1138.40 m/s 313.15 Densities and speeds of sound for binary mixtures of (1,3-dioxolane or 1,4-dioxane) with (2-methyl-1-propanol or 2-methyl-2-propanol) at the temperatures 298.15 K and 313.15 K
csound,fluid 1138.00 m/s 313.15 Excess Enthalpy, Density, and Speed of Sound for the Mixtures a-Pinene + 2-Methyl-1-propanol or 2-Methyl-2-propanol at Several Temperatures
csound,fluid 1108.20 m/s 323.15 Excess Enthalpy, Density, and Speed of Sound for the Mixtures a-Pinene + 2-Methyl-1-propanol or 2-Methyl-2-propanol at Several Temperatures
γ 0.02 N/m 298.15 NCMS SOLV-DB

Datasets

  1. Mass density, kg/m3 (2)
  2. Speed of sound, m/s (1)

Mass density, kg/m3

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
283.15 89.40 809.726
283.16 289.90 810.056
283.15 478.20 810.123
283.15 489.90 810.142
283.15 930.20 810.437
283.15 1027.30 810.557
283.15 2172.10 811.348
283.15 2992.90 811.865
283.15 4993.80 813.245
283.15 6906.90 814.669
283.15 8995.70 816.167
283.15 10003.00 816.885
283.15 12183.00 818.287
283.15 14910.00 820.439
283.15 17915.00 822.056
283.15 20110.00 823.875
283.15 22168.00 825.177
283.15 24886.00 826.625
283.15 27713.00 828.29
283.15 30148.00 829.717
283.15 32117.00 830.745
283.15 33086.00 831.522
283.15 33288.00 831.507
283.15 34077.00 832.073
283.15 35107.00 832.469
283.15 38030.00 834.322
283.16 39967.00 835.34
283.16 41406.00 835.909
283.15 44591.00 837.752
283.16 48034.00 839.7
283.16 49830.00 840.462
283.16 51952.00 841.796
283.15 54994.00 843.308
283.15 57756.00 844.723
283.15 59886.00 845.575
283.15 61822.00 846.524
283.15 64894.00 848.158
283.16 66072.00 848.566
288.15 85.30 806.159
288.15 351.10 806.381
288.16 549.30 806.494
288.15 718.60 806.519
288.15 928.30 806.632
288.15 1132.30 807.006
288.15 1931.60 807.42
288.15 3433.90 808.429
288.15 5023.90 809.62
288.15 6893.90 810.983
288.15 8406.40 812.175
288.16 9959.10 813.184
288.15 12498.00 814.345
288.15 13061.00 815.035
288.15 15159.00 815.414
288.15 16159.00 816.818
288.15 17078.00 817.715
288.15 19062.00 818.283
288.15 20120.00 819.399
288.15 21983.00 820.3
288.15 22948.00 821.319
288.15 24955.00 821.837
288.16 27092.00 823.174
288.16 29078.00 824.509
288.15 31002.00 825.774
288.16 33729.00 826.936
288.15 36056.00 828.477
288.15 38602.00 829.859
288.15 40698.00 831.363
288.15 42984.00 832.313
288.15 44991.00 833.694
288.15 46862.00 834.848
288.15 49740.00 835.692
288.15 53748.00 837.321
288.15 55203.00 839.369
288.16 57016.00 840.129
288.15 60810.00 841.135
288.16 62338.00 843.086
288.15 65611.00 844.144
293.15 63.40 802.054
293.15 194.50 802.316
293.16 310.40 802.406
293.16 463.50 802.612
293.15 662.60 802.599
293.16 1059.70 802.921
293.16 2037.10 803.747
293.16 2922.00 804.089
293.16 3431.50 804.593
293.16 5298.80 805.894
293.15 5367.80 806.019
293.15 5979.30 806.327
293.16 7111.40 807.238
293.15 8031.40 807.842
293.16 9968.50 809.474
293.15 12279.00 811.587
293.16 14057.00 812.743
293.15 16110.00 814.191
293.15 18001.00 815.385
293.16 20853.00 817.066
293.16 22118.00 818.157
293.16 24057.00 819.188
293.16 25922.00 820.412
293.16 27187.00 821.228
293.15 30253.00 822.999
293.15 32967.00 824.811
293.16 34602.00 825.683
293.16 38051.00 827.567
293.16 40103.00 828.763
293.15 42984.00 830.218
293.15 44913.00 831.278
293.15 47933.00 833.008
293.15 50078.00 834.047
293.16 52135.00 835.387
293.16 55036.00 836.79
293.16 58004.00 838.271
293.16 60107.00 839.502
293.16 62061.00 840.325
293.16 66037.00 842.335
298.15 122.40 798.281
298.15 162.60 798.371
298.15 405.50 798.562
298.15 632.80 798.678
298.15 956.40 798.832
298.16 1152.20 799.011
298.16 2046.30 799.798
298.16 3021.10 800.42
298.16 5107.40 801.927
298.15 6988.80 803.491
298.16 9044.30 804.777
298.16 9996.80 805.681
298.16 11947.00 807.14
298.15 14555.00 809.311
298.15 18284.00 812.068
298.15 20164.00 813.104
298.15 22781.00 814.894
298.15 25076.00 816.275
298.15 27604.00 817.904
298.15 30046.00 819.519
298.15 32326.00 821.055
298.16 33072.00 821.357
298.15 33317.00 821.248
298.16 34997.00 822.338
298.16 37948.00 823.936
298.16 39972.00 825.207
298.16 41983.00 826.345
298.15 44911.00 827.946
298.16 48045.00 829.528
298.16 49997.00 830.783
298.16 52020.00 832.399
298.16 54851.00 833.381
298.16 57898.00 835.245
298.15 60006.00 836.063
298.15 62079.00 837.121
298.15 65330.00 838.566
298.15 66093.00 839.052
303.15 50.60 793.736
303.16 270.10 793.901
303.16 464.40 794.084
303.16 779.60 794.287
303.15 974.40 794.496
303.15 1922.50 795.367
303.16 2945.00 796.031
303.16 4911.20 797.923
303.16 7058.60 799.569
303.15 9012.30 801.25
303.15 10062.00 802.346
303.16 12047.00 803.47
303.15 14908.00 805.823
303.15 18109.00 808.133
303.15 20042.00 809.402
303.16 22055.00 811.092
303.15 25084.00 812.578
303.16 28094.00 815.049
303.15 30167.00 816.191
303.15 32070.00 817.319
303.15 33147.00 817.694
303.16 32939.00 817.604
303.16 34037.00 818.139
303.15 35162.00 818.815
303.15 38019.00 820.574
303.15 39970.00 821.716
303.15 42004.00 823.024
303.15 45033.00 824.95
303.16 48317.00 826.769
303.15 49864.00 827.592
303.15 52115.00 829.036
303.15 55239.00 830.776
303.15 58089.00 832.479
303.15 60079.00 833.282
303.15 62294.00 834.706
303.15 65137.00 835.715
303.16 66124.00 836.43
308.15 96.70 791.579
308.15 250.60 791.714
308.15 562.20 791.995
308.16 770.20 792.158
308.15 991.90 792.349
308.16 2101.20 793.3
308.16 3195.10 794.224
308.15 5219.30 795.881
308.16 7083.00 797.398
308.16 9108.00 799.011
308.15 10282.00 799.926
308.16 12379.00 801.538
308.15 15083.00 803.575
308.16 18161.00 805.827
308.16 20006.00 807.165
308.16 22192.00 808.686
308.16 25100.00 810.705
308.16 27887.00 812.568
308.16 30041.00 813.99
308.16 31933.00 815.242
308.16 33077.00 815.959
308.15 32866.00 815.75
308.16 34026.00 816.482
308.15 35203.00 817.171
308.16 35193.00 817.245
308.16 38088.00 818.995
308.16 40106.00 820.225
308.16 42282.00 821.541
308.16 45145.00 823.251
308.15 48031.00 824.96
308.16 50089.00 826.126
308.16 52047.00 827.233
308.15 55094.00 828.952
308.16 58085.00 830.585
308.15 60161.00 831.729
308.15 62192.00 832.798
308.16 65217.00 834.405
308.15 66004.00 834.804
313.15 82.90 787.4
313.15 316.80 787.607
313.15 491.80 787.767
313.15 890.90 788.108
313.15 981.50 788.182
313.15 1939.60 789.038
313.15 2951.00 789.905
313.15 4889.10 791.537
313.15 6856.50 793.195
313.15 8886.90 794.841
313.15 10029.00 795.77
313.15 11886.00 797.214
313.15 14927.00 799.577
313.15 17845.00 801.775
313.15 20040.00 803.389
313.15 21942.00 804.76
313.15 24894.00 806.85
313.15 28132.00 809.095
313.15 29974.00 810.333
313.15 32058.00 811.716
313.16 33053.00 812.371
313.16 33131.00 812.356
313.16 34040.00 812.94
313.15 35162.00 813.664
313.15 37952.00 815.444
313.15 40011.00 816.732
313.15 41939.00 817.878
313.15 45098.00 819.95
313.15 47966.00 821.512
313.15 49918.00 822.65
313.15 52024.00 823.857
313.15 54951.00 825.557
313.15 58062.00 827.336
313.15 60202.00 828.515
313.16 62187.00 829.599
313.15 65050.00 831.15
313.15 66082.00 831.7
318.16 128.50 783.253
318.15 368.30 783.457
318.15 589.40 783.667
318.16 858.20 783.902
318.16 1069.50 784.105
318.16 1979.10 784.923
318.16 2997.40 785.79
318.16 4942.60 787.513
318.16 6987.20 789.27
318.16 8967.50 790.929
318.15 9887.60 791.657
318.16 11870.00 793.265
318.16 14863.00 795.639
318.16 17735.00 797.848
318.16 19860.00 799.438
318.16 21987.00 801.004
318.16 25193.00 803.357
318.16 27823.00 805.216
318.16 30119.00 806.799
318.16 32145.00 808.205
318.15 33128.00 808.894
318.15 33065.00 808.852
318.16 34164.00 809.488
318.15 35190.00 810.134
318.16 38074.00 812.009
318.16 40048.00 813.265
318.16 41997.00 814.496
318.16 45096.00 816.426
318.15 48088.00 818.249
318.16 50173.00 819.491
318.15 52184.00 820.67
318.16 55235.00 822.46
318.16 58075.00 824.084
318.15 60194.00 825.273
318.15 62260.00 826.409
318.15 65194.00 828.017
318.15 66060.00 828.484
323.15 62.10 778.89
323.15 338.00 779.159
323.15 557.50 779.374
323.15 917.30 779.697
323.16 1117.80 779.897
323.15 2125.40 780.833
323.15 3154.80 781.778
323.15 5126.40 783.557
323.15 7366.80 785.517
323.15 9081.60 787.01
323.15 10156.00 787.907
323.15 12167.00 789.544
323.15 15030.00 791.876
323.15 18076.00 794.274
323.15 19932.00 795.694
323.15 22079.00 797.333
323.15 25085.00 799.541
323.15 28006.00 801.644
323.15 30029.00 803.084
323.15 31969.00 804.431
323.15 32903.00 805.081
323.15 33102.00 805.154
323.15 33950.00 805.707
323.15 34958.00 806.425
323.15 37883.00 808.369
323.15 39891.00 809.68
323.15 42065.00 811.076
323.15 44846.00 812.852
323.16 47886.00 814.721
323.15 49935.00 815.968
323.15 52064.00 817.249
323.15 54897.00 818.944
323.15 57818.00 820.634
323.15 59855.00 821.787
323.15 61856.00 822.928
323.15 64838.00 824.6
323.15 65957.00 825.209
328.15 96.50 774.907
328.15 395.80 775.157
328.16 515.00 775.262
328.15 904.10 775.603
328.15 1030.60 775.74
328.16 2069.70 776.794
328.15 2999.30 777.646
328.15 5042.00 779.515
328.16 6936.70 781.257
328.16 8874.20 782.985
328.15 10121.00 784.077
328.15 11905.00 785.621
328.16 14954.00 788.149
328.16 17891.00 790.513
328.16 20040.00 792.21
328.16 22054.00 793.773
328.15 24953.00 795.929
328.15 27874.00 798.098
328.15 29949.00 799.588
328.15 31948.00 800.996
328.16 33018.00 801.745
328.15 33061.00 801.681
328.15 34111.00 802.415
328.15 34984.00 803.007
328.15 37913.00 805.001
328.16 39966.00 806.346
328.15 41958.00 807.674
328.15 44806.00 809.5
328.16 47820.00 811.414
328.16 49817.00 812.637
328.16 52099.00 814.145
328.15 55150.00 815.995
328.15 58100.00 817.75
328.15 60045.00 818.881
328.15 62082.00 820.048
328.16 64955.00 821.692
328.15 66095.00 822.334
333.15 95.70 770.629
333.16 295.90 770.818
333.16 574.50 771.11
333.15 913.60 771.467
333.16 1069.50 771.621
333.16 2110.60 772.649
333.16 3100.00 773.622
333.16 5034.00 775.464
333.15 6965.60 777.259
333.15 8937.30 779.076
333.15 9995.10 780.005
333.15 11970.00 781.72
333.15 14915.00 784.255
333.16 17954.00 786.777
333.16 19985.00 788.397
333.15 22033.00 790.027
333.16 24923.00 792.261
333.16 27922.00 794.514
333.15 29996.00 796.045
333.15 31986.00 797.49
333.15 32928.00 798.124
333.16 33031.00 798.137
333.16 34001.00 798.837
333.16 35030.00 799.567
333.16 37925.00 801.558
333.16 39862.00 802.861
333.15 41792.00 804.162
333.16 44782.00 806.126
333.15 47830.00 808.087
333.15 49895.00 809.38
333.15 51876.00 810.61
333.15 54830.00 812.44
333.15 58116.00 814.429
333.15 59975.00 815.509
333.15 61974.00 816.676
333.15 65057.00 818.467
333.15 66042.00 819.039
338.15 72.50 765.803
338.15 267.10 766.009
338.15 496.50 766.255
338.15 821.30 766.6
338.15 1007.70 766.796
338.15 2012.40 767.824
338.15 3039.10 768.845
338.16 5091.10 770.879
338.15 7018.50 772.739
338.15 8987.60 774.596
338.15 10054.00 775.578
338.16 12131.00 777.462
338.16 15171.00 780.113
338.15 18105.00 782.627
338.16 20167.00 784.349
338.15 22120.00 785.947
338.16 25290.00 788.465
338.15 28029.00 790.565
338.16 30041.00 792.069
338.15 32010.00 793.527
338.15 32776.00 794.103
338.15 32995.00 794.184
338.15 33922.00 794.869
338.16 35102.00 795.7
338.15 38056.00 797.798
338.16 39987.00 799.156
338.15 42127.00 800.629
338.16 45109.00 802.623
338.15 48090.00 804.572
338.15 50121.00 805.906
338.15 52094.00 807.168
338.15 55116.00 809.055
338.15 58010.00 810.837
338.15 60191.00 812.149
338.15 62244.00 813.373
338.15 65243.00 815.143
338.15 65986.00 815.583
338.15 66355.00 815.805
343.15 55.60 761.239
343.15 101.80 761.279
343.15 277.30 761.484
343.15 487.70 761.699
343.15 881.60 762.13
343.15 1037.00 762.294
343.15 1941.40 763.263
343.15 3000.30 764.362
343.15 4957.00 766.378
343.15 6956.10 768.377
343.15 8969.50 770.304
343.15 10003.00 771.264
343.15 11997.00 773.149
343.15 14895.00 775.758
343.15 17840.00 778.358
343.15 20135.00 780.417
343.15 21925.00 781.908
343.15 24920.00 784.349
343.15 27949.00 786.755
343.15 29863.00 788.238
343.15 31874.00 789.777
343.15 32981.00 790.602
343.15 32927.00 790.544
343.15 34026.00 791.305
343.15 35028.00 792.011
343.15 38080.00 794.257
343.15 39908.00 795.53
343.15 41973.00 796.98
343.15 44972.00 799.034
343.15 47997.00 801.072
343.15 50016.00 802.401
343.15 52079.00 803.724
343.15 54997.00 805.581
343.15 57987.00 807.46
343.16 60015.00 808.691
343.15 62074.00 809.959
343.15 65051.00 811.734
343.15 66170.00 812.401
348.15 94.00 756.672
348.15 293.80 756.914
348.15 481.90 757.128
348.15 763.50 757.435
348.15 1011.00 757.701
348.15 1981.10 758.826
348.15 3073.20 759.88
348.15 5089.90 762.131
348.15 7034.60 764.092
348.15 9052.50 766.106
348.15 9991.30 767.026
348.16 12060.00 769.03
348.15 15042.00 771.822
348.15 17922.00 774.408
348.15 19893.00 776.137
348.15 22033.00 777.985
348.15 22381.00 778.265
348.16 25066.00 780.513
348.15 28023.00 782.927
348.15 29922.00 784.471
348.16 32007.00 786.046
348.16 32760.00 786.619
348.16 32941.00 786.66
348.15 33999.00 787.493
348.15 34980.00 788.228
348.15 37995.00 790.467
348.15 40072.00 791.973
348.15 41992.00 793.388
348.15 45082.00 795.525
348.15 48031.00 797.589
348.16 50014.00 798.878
348.15 52067.00 800.261
348.15 55099.00 802.242
348.16 58146.00 804.186
348.15 60084.00 805.42
348.15 62302.00 806.758
348.15 65219.00 808.569
348.15 66250.00 809.201
353.15 98.10 752.221
353.15 305.80 752.433
353.15 384.00 752.511
353.15 558.50 752.696
353.15 929.40 753.125
353.15 1073.70 753.289
353.15 2082.70 754.432
353.15 3025.90 755.465
353.15 5017.90 757.656
353.15 6957.80 759.69
353.15 8976.60 761.781
353.15 9990.30 762.812
353.15 11934.00 764.803
353.15 14917.00 767.603
353.15 18020.00 770.471
353.15 19983.00 772.259
353.15 22060.00 773.965
353.15 24899.00 776.429
353.15 27951.00 778.961
353.15 29947.00 780.584
353.15 31942.00 782.185
353.15 32982.00 782.978
353.15 33037.00 783.002
353.15 33907.00 783.604
353.15 35053.00 784.493
353.15 37939.00 786.664
353.15 39830.00 788.076
353.15 41863.00 789.556
353.15 44753.00 791.642
353.15 47880.00 793.816
353.15 49780.00 795.14
353.15 51876.00 796.535
353.15 55023.00 798.765
353.15 55678.00 799.178
353.15 57869.00 800.594
353.15 59971.00 801.962
353.15 62015.00 803.245
353.15 64989.00 805.09
353.15 66151.00 805.82
358.15 91.60 747.694
358.15 304.90 747.895
358.15 517.30 748.147
358.15 850.10 748.568
358.15 1095.50 748.835
358.15 2101.60 750.029
358.15 3210.60 751.303
358.15 5324.20 753.465
358.15 7190.10 755.483
358.15 9074.30 757.505
358.15 10165.00 758.644
358.15 12208.00 760.738
358.15 13986.00 762.552
358.15 15000.00 763.577
358.15 17866.00 766.293
358.15 20104.00 768.379
358.16 22005.00 770.073
358.16 25079.00 772.781
358.15 27962.00 775.177
358.15 30131.00 776.699
358.15 32076.00 778.299
358.15 33039.00 779.08
358.15 32938.00 778.904
358.15 33914.00 779.672
358.15 34978.00 780.53
358.15 37986.00 782.876
358.15 39996.00 784.402
358.15 42079.00 785.976
358.15 45119.00 788.207
358.15 48100.00 790.343
358.15 49987.00 791.672
358.15 52101.00 793.112
358.15 54983.00 795.084
358.15 58017.00 797.106
358.15 60055.00 798.438
358.15 62083.00 799.766
358.15 65016.00 801.626
358.15 66339.00 802.467
363.15 53.20 742.307
363.15 125.50 742.405
363.15 320.30 742.647
363.15 562.50 742.935
363.15 892.50 743.339
363.15 1001.30 743.446
363.15 1911.60 744.576
363.15 2977.30 745.832
363.15 4957.50 748.169
363.15 6937.40 750.436
363.15 8892.90 752.564
363.15 10033.00 753.801
363.15 11914.00 755.769
363.15 14908.00 758.826
363.15 17925.00 761.773
363.15 19995.00 763.754
363.15 21953.00 765.578
363.15 24962.00 768.273
363.15 27932.00 770.858
363.15 30163.00 772.879
363.15 32029.00 774.439
363.15 33151.00 775.369
363.15 33315.00 775.421
363.15 34086.00 776.049
363.15 35189.00 776.934
363.15 37932.00 779.076
363.15 40070.00 780.754
363.15 41883.00 782.107
363.15 44755.00 784.308
363.15 48054.00 786.713
363.15 50037.00 788.134
363.15 51977.00 789.492
363.15 55048.00 791.627
363.15 57990.00 793.615
363.15 60071.00 794.972
363.15 62073.00 796.302
363.15 64996.00 798.178
363.15 66050.00 798.847
Reference
Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
298.15 1.53 797.775
Reference

Speed of sound, m/s

Operational condition: Frequency, MHz = 8 (Liquid)

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Speed of sound, m/s - Liquid
253.15 102.00 1347.322
253.15 5144.00 1373.695
253.15 10257.00 1399.134
253.15 15122.00 1422.242
253.15 20400.00 1446.625
253.15 25315.00 1467.969
253.15 30039.00 1488.704
273.15 105.00 1274.213
273.15 5154.00 1302.778
273.15 10139.00 1329.437
273.15 15072.00 1354.721
273.15 20215.00 1379.951
273.15 25138.00 1403.158
273.15 30242.00 1426.375
293.15 102.00 1204.925
293.15 5004.00 1234.867
293.15 10097.00 1264.152
293.15 15140.00 1291.722
293.15 20220.00 1318.237
293.15 25063.00 1342.456
293.15 30100.00 1366.71
313.15 104.00 1138.14
313.15 5135.00 1171.059
313.15 10050.00 1201.432
313.15 15190.00 1231.544
313.15 20126.00 1259.038
313.15 25019.00 1285.053
313.15 30259.00 1311.678
333.15 100.00 1071.814
333.15 5187.00 1108.004
333.15 10181.00 1141.267
333.15 15331.00 1173.58
333.15 20135.00 1202.01
333.15 25174.00 1230.377
333.15 30144.00 1257.018
353.15 104.00 1004.081
353.15 5055.00 1042.847
353.15 10093.00 1079.408
353.15 15238.00 1114.154
353.15 20157.00 1145.379
353.15 25111.00 1175.116
353.15 30108.00 1203.555
Reference

Correlations

Property Value Unit Temperature (K) Source
Cp,gas [95.69; 263.37] J/mol×K [255.37; 1200.00] 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 A2.08570e+01
Coefficient B-2.75260e+02
Coefficient C5.22924e+00
Coefficient D7.04780e-04
Coefficient E-2.46200e-07
Temperature range, min.255.37
Temperature range, max.1200.00
Cp,gas 95.69 J/mol×K 255.37 Calculated Property
Cp,gas 129.42 J/mol×K 360.33 Calculated Property
Cp,gas 156.81 J/mol×K 465.29 Calculated Property
Cp,gas 179.77 J/mol×K 570.25 Calculated Property
Cp,gas 199.47 J/mol×K 675.21 Calculated Property
Cp,gas 216.52 J/mol×K 780.16 Calculated Property
Cp,gas 231.30 J/mol×K 885.12 Calculated Property
Cp,gas 243.97 J/mol×K 990.08 Calculated Property
Cp,gas 254.65 J/mol×K 1095.04 Calculated Property
Cp,gas 263.37 J/mol×K 1200.00 Calculated Property
Property Value Unit Temperature (K) Source
Cp,liquid [127.09; 271.08] J/mol×K [165.15; 403.87] 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 A1.14500e+02
Coefficient B8.44650e+02
Coefficient C-1.05831e+01
Coefficient D5.87660e-02
Coefficient E-6.24640e-05
Temperature range, min.165.15
Temperature range, max.403.87
Cp,liquid 127.09 J/mol×K 165.15 Calculated Property
Cp,liquid 130.83 J/mol×K 191.67 Calculated Property
Cp,liquid 137.53 J/mol×K 218.20 Calculated Property
Cp,liquid 147.91 J/mol×K 244.72 Calculated Property
Cp,liquid 162.69 J/mol×K 271.25 Calculated Property
Cp,liquid 182.11 J/mol×K 297.77 Calculated Property
Cp,liquid 205.41 J/mol×K 324.30 Calculated Property
Cp,liquid 230.45 J/mol×K 350.82 Calculated Property
Cp,liquid 253.74 J/mol×K 377.35 Calculated Property
Cp,liquid 271.08 J/mol×K 403.87 Calculated Property
Property Value Unit Temperature (K) Source
η [0.2536623; 0.0000464] Pa×s [210.93; 544.26] 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-1.07966e+02
Coefficient B6.19974e+03
Coefficient C1.45721e+01
Coefficient D-1.75520e-05
Coefficient E2.00000e+00
Temperature range, min.210.93
Temperature range, max.544.26
η 0.2536623 Pa×s 210.93 Calculated Property
η 0.0246530 Pa×s 247.97 Calculated Property
η 0.0051442 Pa×s 285.00 Calculated Property
η 0.0016851 Pa×s 322.04 Calculated Property
η 0.0007259 Pa×s 359.08 Calculated Property
η 0.0003697 Pa×s 396.11 Calculated Property
η 0.0002081 Pa×s 433.15 Calculated Property
η 0.0001238 Pa×s 470.19 Calculated Property
η 0.0000756 Pa×s 507.22 Calculated Property
η 0.0000464 Pa×s 544.26 Calculated Property
Property Value Unit Temperature (K) Source
ΔvapH [62.71; 15.40] kJ/mol [165.15; 527.66] 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 A6.14110e+01
Coefficient B-6.77030e-01
Coefficient C2.68840e+00
Coefficient D-2.34160e+00
Coefficient E7.59420e-01
Critical temperature, Tc (K)5.47780e+02
Temperature range, min.165.15
Temperature range, max.527.66
ΔvapH 62.71 kJ/mol 165.15 Calculated Property
ΔvapH 60.21 kJ/mol 205.43 Calculated Property
ΔvapH 56.96 kJ/mol 245.71 Calculated Property
ΔvapH 53.12 kJ/mol 285.99 Calculated Property
ΔvapH 48.80 kJ/mol 326.27 Calculated Property
ΔvapH 44.02 kJ/mol 366.54 Calculated Property
ΔvapH 38.76 kJ/mol 406.82 Calculated Property
ΔvapH 32.80 kJ/mol 447.10 Calculated Property
ΔvapH 25.64 kJ/mol 487.38 Calculated Property
ΔvapH 15.40 kJ/mol 527.66 Calculated Property
Property Value Unit Temperature (K) Source
Pvap [1.33; 202.65] kPa [297.75; 401.38] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.44742e+01
Coefficient B-2.68120e+03
Coefficient C-1.08758e+02
Temperature range, min.297.75
Temperature range, max.401.38
Pvap 1.33 kPa 297.75 Calculated Property
Pvap 3.01 kPa 309.26 Calculated Property
Pvap 6.22 kPa 320.78 Calculated Property
Pvap 11.94 kPa 332.29 Calculated Property
Pvap 21.48 kPa 343.81 Calculated Property
Pvap 36.60 kPa 355.32 Calculated Property
Pvap 59.45 kPa 366.84 Calculated Property
Pvap 92.65 kPa 378.35 Calculated Property
Pvap 139.24 kPa 389.87 Calculated Property
Pvap 202.65 kPa 401.38 Calculated Property
Pvap [1.26e-09; 4508.05] kPa [165.15; 547.78] 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 A1.67129e+02
Coefficient B-1.22888e+04
Coefficient C-2.22393e+01
Coefficient D1.31856e-05
Coefficient E2.00000e+00
CommentRange stopped at Tc; ChemSep gives it to 547.8 K.
Temperature range, min.165.15
Temperature range, max.547.78
Pvap 1.26e-09 kPa 165.15 Calculated Property
Pvap 3.92e-05 kPa 207.66 Calculated Property
Pvap 0.02 kPa 250.18 Calculated Property
Pvap 0.97 kPa 292.69 Calculated Property
Pvap 13.94 kPa 335.21 Calculated Property
Pvap 90.46 kPa 377.72 Calculated Property
Pvap 354.81 kPa 420.24 Calculated Property
Pvap 1002.18 kPa 462.75 Calculated Property
Pvap 2280.99 kPa 505.27 Calculated Property
Pvap 4508.05 kPa 547.78 Calculated Property
Pvap [4.46e-10; 4532.42] kPa [165.15; 547.73] KDB Vapor Pressure Data Show Hide
Equationln(Y) = A + B/T + C·ln(T) + D·T² + E/T²
Y is Pvap in kPa, T in K
Coefficient A2.14566e+02
Coefficient B-1.41062e+04
Coefficient C-2.96193e+01
Coefficient D2.12663e-05
Coefficient E0.00000e+00
Temperature range, min.165.15
Temperature range, max.547.73
Pvap 4.46e-10 kPa 165.15 Calculated Property
Pvap 2.77e-05 kPa 207.66 Calculated Property
Pvap 0.02 kPa 250.17 Calculated Property
Pvap 0.98 kPa 292.68 Calculated Property
Pvap 14.06 kPa 335.19 Calculated Property
Pvap 88.93 kPa 377.69 Calculated Property
Pvap 339.80 kPa 420.20 Calculated Property
Pvap 949.79 kPa 462.71 Calculated Property
Pvap 2193.06 kPa 505.22 Calculated Property
Pvap 4532.42 kPa 547.73 Calculated Property
Pvap [381.65; 4276.97] kPa [422.64; 547.71] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.47380e+01
Coefficient B-2.90230e+03
Coefficient C-9.25880e+01
ReferenceAmbrose and Townsend, 1963, 3
CommentCoefficents calculated by NIST from author's data.
Temperature range, min.422.64
Temperature range, max.547.71
Pvap 381.65 kPa 422.64 Calculated Property
Pvap 544.46 kPa 436.54 Calculated Property
Pvap 755.58 kPa 450.43 Calculated Property
Pvap 1023.18 kPa 464.33 Calculated Property
Pvap 1355.62 kPa 478.23 Calculated Property
Pvap 1761.26 kPa 492.12 Calculated Property
Pvap 2248.35 kPa 506.02 Calculated Property
Pvap 2824.94 kPa 519.92 Calculated Property
Pvap 3498.72 kPa 533.81 Calculated Property
Pvap 4276.97 kPa 547.71 Calculated Property
Pvap [33.06; 133.30] kPa [353.36; 388.77] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.48085e+01
Coefficient B-2.84828e+03
Coefficient C-1.01528e+02
ReferenceBiddiscombe, Collerson, et al., 1963, 2
CommentCoefficents calculated by NIST from author's data.
Temperature range, min.353.36
Temperature range, max.388.77
Pvap 33.06 kPa 353.36 Calculated Property
Pvap 39.34 kPa 357.29 Calculated Property
Pvap 46.57 kPa 361.23 Calculated Property
Pvap 54.85 kPa 365.16 Calculated Property
Pvap 64.30 kPa 369.10 Calculated Property
Pvap 75.02 kPa 373.03 Calculated Property
Pvap 87.15 kPa 376.97 Calculated Property
Pvap 100.81 kPa 380.90 Calculated Property
Pvap 116.15 kPa 384.84 Calculated Property
Pvap 133.30 kPa 388.77 Calculated Property
Pvap [381.65; 4276.97] kPa [422.64; 547.71] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.47380e+01
Coefficient B-2.90230e+03
Coefficient C-9.25880e+01
ReferenceAmbrose and Townsend, 1963
CommentCoefficents calculated by NIST from author's data.
Temperature range, min.422.64
Temperature range, max.547.71
Pvap 381.65 kPa 422.64 Calculated Property
Pvap 544.46 kPa 436.54 Calculated Property
Pvap 755.58 kPa 450.43 Calculated Property
Pvap 1023.18 kPa 464.33 Calculated Property
Pvap 1355.62 kPa 478.23 Calculated Property
Pvap 1761.26 kPa 492.12 Calculated Property
Pvap 2248.35 kPa 506.02 Calculated Property
Pvap 2824.94 kPa 519.92 Calculated Property
Pvap 3498.72 kPa 533.81 Calculated Property
Pvap 4276.97 kPa 547.71 Calculated Property
Pvap [33.06; 133.30] kPa [353.36; 388.77] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.48085e+01
Coefficient B-2.84828e+03
Coefficient C-1.01528e+02
ReferenceBiddiscombe, Collerson, et al., 1963
CommentCoefficents calculated by NIST from author's data.
Temperature range, min.353.36
Temperature range, max.388.77
Pvap 33.06 kPa 353.36 Calculated Property
Pvap 39.34 kPa 357.29 Calculated Property
Pvap 46.57 kPa 361.23 Calculated Property
Pvap 54.85 kPa 365.16 Calculated Property
Pvap 64.30 kPa 369.10 Calculated Property
Pvap 75.02 kPa 373.03 Calculated Property
Pvap 87.15 kPa 376.97 Calculated Property
Pvap 100.81 kPa 380.90 Calculated Property
Pvap 116.15 kPa 384.84 Calculated Property
Pvap 133.30 kPa 388.77 Calculated Property
Property Value Unit Temperature (K) Source
ρl [892.39; 289.14] kg/m3 [165.15; 547.78] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A / B^(1 + (1 − T/C)^D)
Y is ρl in kg/m3, T in K
Coefficient A5.94411e+01
Coefficient B2.45150e-01
Coefficient C5.47810e+02
Coefficient D2.11750e-01
CommentRange stopped at Tc; ChemSep gives it to 547.8 K.
Temperature range, min.165.15
Temperature range, max.547.78
ρl 892.39 kg/m3 165.15 Calculated Property
ρl 864.21 kg/m3 207.66 Calculated Property
ρl 834.12 kg/m3 250.18 Calculated Property
ρl 801.68 kg/m3 292.69 Calculated Property
ρl 766.19 kg/m3 335.21 Calculated Property
ρl 726.57 kg/m3 377.72 Calculated Property
ρl 680.95 kg/m3 420.24 Calculated Property
ρl 625.50 kg/m3 462.75 Calculated Property
ρl 549.63 kg/m3 505.27 Calculated Property
ρl 289.14 kg/m3 547.78 Calculated Property
Property Value Unit Temperature (K) Source
γ [0.03; 0.02] N/m [165.15; 381.15] 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 A4.62454e-02
Coefficient B-7.95000e-05
Coefficient C0.00000e+00
Coefficient D0.00000e+00
Coefficient E0.00000e+00
Temperature range, min.165.15
Temperature range, max.381.15
γ 0.03 N/m 165.15 Calculated Property
γ 0.03 N/m 189.15 Calculated Property
γ 0.03 N/m 213.15 Calculated Property
γ 0.03 N/m 237.15 Calculated Property
γ 0.03 N/m 261.15 Calculated Property
γ 0.02 N/m 285.15 Calculated Property
γ 0.02 N/m 309.15 Calculated Property
γ 0.02 N/m 333.15 Calculated Property
γ 0.02 N/m 357.15 Calculated Property
γ 0.02 N/m 381.15 Calculated Property
γ [0.02; 0.02] N/m [283.15; 380.81] 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-1.04740e-02
Coefficient B-2.25690e+02
Coefficient C-8.81630e-01
Coefficient D-6.93490e-03
Coefficient E3.33370e-06
Temperature range, min.283.15
Temperature range, max.380.81
γ 0.02 N/m 283.15 Calculated Property
γ 0.02 N/m 294.00 Calculated Property
γ 0.02 N/m 304.85 Calculated Property
γ 0.02 N/m 315.70 Calculated Property
γ 0.02 N/m 326.55 Calculated Property
γ 0.02 N/m 337.41 Calculated Property
γ 0.02 N/m 348.26 Calculated Property
γ 0.02 N/m 359.11 Calculated Property
γ 0.02 N/m 369.96 Calculated Property
γ 0.02 N/m 380.81 Calculated Property
Property Value Unit Temperature (K) Source
λgas [0.00; 0.11] W/m×K [165.15; 1000.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A·T^B / (1 + C/T + D/T²)
Y is λgas in W/m×K, T in K
Coefficient A2.18990e+03
Coefficient B9.12220e-01
Coefficient C1.12440e+10
Coefficient D-5.10030e+11
Temperature range, min.165.15
Temperature range, max.1000.00
λgas 0.00 W/m×K 165.15 Calculated Property
λgas 0.01 W/m×K 257.91 Calculated Property
λgas 0.02 W/m×K 350.67 Calculated Property
λgas 0.02 W/m×K 443.43 Calculated Property
λgas 0.04 W/m×K 536.19 Calculated Property
λgas 0.05 W/m×K 628.96 Calculated Property
λgas 0.06 W/m×K 721.72 Calculated Property
λgas 0.08 W/m×K 814.48 Calculated Property
λgas 0.09 W/m×K 907.24 Calculated Property
λgas 0.11 W/m×K 1000.00 Calculated Property
Property Value Unit Temperature (K) Source
λliquid [0.18; 0.09] W/m×K [165.15; 488.71] 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 A-2.76850e-01
Coefficient B3.67220e+01
Coefficient C-1.06890e+00
Coefficient D6.60560e-04
Coefficient E-1.40480e-06
Temperature range, min.165.15
Temperature range, max.488.71
λliquid 0.18 W/m×K 165.15 Calculated Property
λliquid 0.17 W/m×K 201.10 Calculated Property
λliquid 0.16 W/m×K 237.05 Calculated Property
λliquid 0.15 W/m×K 273.00 Calculated Property
λliquid 0.14 W/m×K 308.95 Calculated Property
λliquid 0.13 W/m×K 344.91 Calculated Property
λliquid 0.12 W/m×K 380.86 Calculated Property
λliquid 0.11 W/m×K 416.81 Calculated Property
λliquid 0.10 W/m×K 452.76 Calculated Property
λliquid 0.09 W/m×K 488.71 Calculated Property

Similar Compounds

2-METHYL-1,3-PROPANEDIOL. 1,3-Propanediol, 2-(hydroxymethyl)-. Propanol, 3,3,3-trichloro-2-methyl-. 1-Propanol. 1-Propanol, 2,2-dimethyl-. Isobutyl nitrite. 1-Butanol, 2,3-dimethyl-. 2-methylbutanol-d-3. 2-methylbutanol-d-9. 1-Butanol, 2-methyl-. 1-Butanol, 2-methyl-, (S)-. Cyclopropyl carbinol. Oxetane, 3-methyl. 3-Mercapto-2-methylpropanol. Propane, 1-methoxy-2-methyl-.

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Mixtures

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Sources

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