Chemical Properties of 2-Butanol (CAS 78-92-2)

2-Butanol

InChI
InChI=1S/C4H10O/c1-3-4(2)5/h4-5H,3H2,1-2H3
InChI Key
BTANRVKWQNVYAZ-UHFFFAOYSA-N
Formula
C4H10O
SMILES
CCC(C)O
Molecular Weight1
74.12
CAS
78-92-2
Other Names
  • (RS)-2-butanol
  • 1-Methyl propanol
  • 1-Methyl-1-propanol
  • 1-Methylpropyl alcohol
  • 2-Butanol, (.+/-.)-
  • 2-Butyl alcohol
  • 2-Hydroxybutane
  • Alcool butylique secondaire
  • Butane, 2-hydroxy-
  • Butanol secondaire
  • Butanol-2
  • Butylene hydrate
  • CCS 301
  • DL-2-butanol
  • DL-sec-Butanol
  • Ethyl methyl carbinol
  • METHYLETHYLCARBINOL
  • Methyl ethyl carbinol
  • NSC 25499
  • butan-2-ol
  • dl-sec-butyl alcohol
  • n-Butan-2-ol
  • s-Butanol
  • s-Butyl alcohol
  • sec-C4H9OH
  • sec-butanol
  • sec-butyl alcohol
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Contents

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

Physical Properties

Property Value Unit Source
ω [0.5740; 0.5770]   Show Hide
ω 0.5760 PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω 0.5740 ChemSep v8.3 pure component data Compiled value
ω 0.5770 KDB
PAff 815.00 kJ/mol NIST
Tig [678.15; 679.26] K Show Hide
Tig 679.26 K KDB
Tig 678.15 K NCMS SOLV-DB
BasG 784.60 kJ/mol NIST
ΔcH°liquid [-2660.60; -2660.59] kJ/mol Show Hide
ΔcH°liquid -2660.60 ± 0.54 kJ/mol NIST
ΔcH°liquid -2660.60 ± 0.92 kJ/mol NIST
ΔcH°liquid -2660.59 ± 0.18 kJ/mol NIST
Cp,liquid 197.80 J/mol×K Partial Molar Heat Capacities and Partial Molar Volumes of All of the Isomeric (C3 to C5) Alkanols at Infinite Dilution in Water at 298.15 K
μ [1.66; 1.70] debye Show Hide
μ 1.66 debye ChemSep v8.3 pure component data Compiled value
μ 1.70 debye KDB
η [0.0029070; 0.0031028] Pa×s Show Hide
η 0.0029070 Pa×s Speeds of sound, isentropic compressibilities, viscosities and excess molar volumes of binary mixtures of methylcyclohexane + 2-alkanols or ethanol at T = 298.15 K
η 0.0031028 Pa×s Densities and Viscosities of Binary Liquid Mixtures of Trichloroethylene and Tetrachloroethylene with Some Polar and Nonpolar Solvents
εr 16.56 NCMS SOLV-DB
LFL 1.70 % in Air KDB
UFL 9.00 % in Air KDB
Tflash,cc 296.15 K NCMS SOLV-DB
Tflash,oc 297.04 K KDB
ΔfG° [-169.60; -167.70] kJ/mol Show Hide
ΔfG° -169.60 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfG° -167.70 kJ/mol KDB
Rg 3.1820 KDB
ΔfH°gas [-293.10; -292.70] kJ/mol Show Hide
ΔfH°gas -292.90 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfH°gas -292.80 kJ/mol KDB
ΔfH°gas -293.10 kJ/mol NIST
ΔfH°gas -293.00 ± 1.50 kJ/mol NIST
ΔfH°gas -292.70 ± 0.30 kJ/mol NIST
ΔfH°liquid [-342.70; -342.60] kJ/mol Show Hide
ΔfH°liquid -342.70 ± 0.59 kJ/mol NIST
ΔfH°liquid -342.60 ± 0.92 kJ/mol NIST
ΔfH°liquid -342.60 ± 0.30 kJ/mol NIST
ΔfusH° 6.68 kJ/mol Joback Calculated Property
ΔvapH° [41.70; 49.86] kJ/mol Show Hide
ΔvapH° 49.66 kJ/mol NCMS SOLV-DB
ΔvapH° 49.81 kJ/mol NIST
ΔvapH° 46.20 kJ/mol NIST
ΔvapH° 49.79 ± 0.02 kJ/mol NIST
ΔvapH° 49.74 ± 0.02 kJ/mol NIST
ΔvapH° 49.70 ± 0.10 kJ/mol NIST
ΔvapH° 49.66 ± 0.08 kJ/mol NIST
ΔvapH° 48.50 kJ/mol NIST
ΔvapH° 49.45 kJ/mol NIST
ΔvapH° Outlier 41.70 ± 0.20 kJ/mol NIST
ΔvapH° 49.86 ± 0.03 kJ/mol NIST
IE [9.88; 10.35] eV Show Hide
IE 9.88 ± 0.03 eV NIST
IE 9.88 ± 0.03 eV NIST
IE 9.88 ± 0.07 eV NIST
IE 9.88 eV NIST
IE 9.88 eV NIST
IE 10.23 eV NIST
IE 10.35 ± 0.03 eV NIST
log10WS [0.43; 0.47]   Show Hide
log10WS 0.43 Aq. Solubility Prediction
log10WS 0.47 Estimated Solubility
logPoct/wat 0.610 NCMS SOLV-DB
McVol 73.090 ml/mol McGowan Calculated Property
NFPA Fire 3 NCMS SOLV-DB
NFPA Health 1 NCMS SOLV-DB
NFPA Safety 0 NCMS SOLV-DB
Pc [4179.00; 4210.00] kPa Show Hide
Pc 4202.00 kPa IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Pc 4194.86 kPa PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc 4179.00 kPa ChemSep v8.3 pure component data Compiled value
Pc 4202.00 kPa KDB
Pc 4200.00 ± 20.00 kPa NIST
Pc 4210.00 kPa NIST
Pc 4203.00 ± 20.00 kPa NIST
Pc 4203.00 ± 20.00 kPa NIST
Pc 4179.00 kPa NIST
Pc 4194.00 kPa NIST
Ptriple 3.17e-09 kPa ChemSep v8.3 pure component data Compiled value
ρc [275.51; 275.73] kg/m3 Show Hide
ρc 275.73 ± 1.48 kg/m3 NIST
ρc 275.73 kg/m3 NIST
ρc 275.51 kg/m3 NIST
Inp [553.00; 628.00]   Show Hide
Inp 605.00 NIST
Inp 577.00 NIST
Inp Outlier 555.00 NIST
Inp 605.00 NIST
Inp 577.00 NIST
Inp 605.00 NIST
Inp 577.00 NIST
Inp 585.00 NIST
Inp 586.00 NIST
Inp 569.00 NIST
Inp 570.00 NIST
Inp 565.00 NIST
Inp 565.00 NIST
Inp 563.00 NIST
Inp 586.00 NIST
Inp 584.00 NIST
Inp 586.00 NIST
Inp 571.00 NIST
Inp 582.00 NIST
Inp 567.00 NIST
Inp 590.00 NIST
Inp Outlier 553.00 NIST
Inp 563.00 NIST
Inp 576.00 NIST
Inp 612.00 NIST
Inp 603.00 NIST
Inp 602.00 NIST
Inp 591.00 NIST
Inp 600.60 NIST
Inp 602.20 NIST
Inp 565.00 NIST
Inp 603.00 NIST
Inp 586.00 NIST
Inp 565.00 NIST
Inp 606.00 NIST
Inp 585.00 NIST
Inp 594.00 NIST
Inp 585.00 NIST
Inp 587.00 NIST
Inp 586.00 NIST
Inp 570.00 NIST
Inp 572.00 NIST
Inp 593.00 NIST
Inp 595.00 NIST
Inp 596.00 NIST
Inp 598.00 NIST
Inp 605.00 NIST
Inp 598.00 NIST
Inp 609.00 NIST
Inp 601.00 NIST
Inp 587.00 NIST
Inp 587.64 NIST
Inp 591.00 NIST
Inp 596.00 NIST
Inp 603.00 NIST
Inp Outlier 628.00 NIST
Inp 610.00 NIST
Inp 586.00 NIST
Inp 586.00 NIST
Inp 597.00 NIST
Inp 586.00 NIST
Inp 591.00 NIST
Inp 602.00 NIST
Inp 582.00 NIST
Inp 589.00 NIST
Inp 613.00 NIST
Inp 596.00 NIST
Inp 585.00 NIST
Inp 608.00 NIST
Inp 585.00 NIST
Inp Outlier 624.00 NIST
Inp 601.00 NIST
Inp 586.00 NIST
Inp 585.00 NIST
Inp 603.00 NIST
Inp 565.00 NIST
Inp 593.00 NIST
Inp 598.00 NIST
Inp 591.00 NIST
Inp 610.00 NIST
Inp 596.00 NIST
Inp 601.00 NIST
Ip [980.00; 1057.00]   Show Hide
Ip 1012.00 NIST
Ip 1044.00 NIST
Ip 1035.00 NIST
Ip 1031.00 NIST
Ip 1048.00 NIST
Ip 1038.00 NIST
Ip 1036.00 NIST
Ip 1048.00 NIST
Ip 1038.00 NIST
Ip 1036.00 NIST
Ip Outlier 1057.00 NIST
Ip 1022.00 NIST
Ip 1020.00 NIST
Ip 1055.00 NIST
Ip 1038.00 NIST
Ip Outlier 992.00 NIST
Ip 1031.00 NIST
Ip 1014.00 NIST
Ip 1041.00 NIST
Ip 1022.00 NIST
Ip 1015.00 NIST
Ip 1036.00 NIST
Ip 1024.00 NIST
Ip 1030.00 NIST
Ip 1037.00 NIST
Ip 1022.00 NIST
Ip 1030.00 NIST
Ip 1021.00 NIST
Ip 1000.00 NIST
Ip 1022.00 NIST
Ip 1044.00 NIST
Ip 1053.00 NIST
Ip 1019.00 NIST
Ip 1039.40 NIST
Ip Outlier 992.00 NIST
Ip 994.00 NIST
Ip 1027.00 NIST
Ip 1027.00 NIST
Ip 1027.00 NIST
Ip 1049.00 NIST
Ip 1041.00 NIST
Ip 1022.00 NIST
Ip 1009.00 NIST
Ip 1034.00 NIST
Ip 1016.00 NIST
Ip 1019.00 NIST
Ip 1000.00 NIST
Ip 1015.00 NIST
Ip 1031.00 NIST
Ip 1035.00 NIST
Ip 1039.00 NIST
Ip 1031.00 NIST
Ip 1029.00 NIST
Ip 1012.00 NIST
Ip 1016.00 NIST
Ip 1015.00 NIST
Ip 1045.00 NIST
Ip 1029.00 NIST
Ip 1019.00 NIST
Ip 1028.00 NIST
Ip 1027.00 NIST
Ip 1032.00 NIST
Ip 1020.00 NIST
Ip 1022.00 NIST
Ip 1022.00 NIST
Ip 998.00 NIST
Ip 998.00 NIST
Ip 1017.00 NIST
Ip 1045.00 NIST
Ip 1022.00 NIST
Ip 1030.00 NIST
Ip 1030.00 NIST
Ip 1046.00 NIST
Ip 1029.00 NIST
Ip Outlier 988.00 NIST
Ip 1000.00 NIST
Ip Outlier 980.00 NIST
Ip 1000.00 NIST
Ip 1022.00 NIST
Ip 1022.00 NIST
Ip 1026.00 NIST
Ip 1001.00 NIST
Ip 1000.00 NIST
Ip 1031.00 NIST
Ip 1012.00 NIST
Ip 1013.00 NIST
Ip 1048.00 NIST
Ip 1031.00 NIST
Ip 1047.00 NIST
Ip 1044.00 NIST
Ip 1019.00 NIST
Ip 1019.00 NIST
Ip 1025.00 NIST
Ip 1044.00 NIST
Ip 1035.00 NIST
Ip 1039.00 NIST
Ip 1025.00 NIST
Ip 1000.00 NIST
Ip 1005.00 NIST
Ip 1031.00 NIST
Ip 1014.00 NIST
Ip 1022.00 NIST
Ip 994.00 NIST
Ip 1041.00 NIST
Ip 1019.00 NIST
Ip 1045.00 NIST
Ip 1024.00 NIST
S°gas 355.37 J/mol×K NIST
S°liquid [213.10; 214.70] J/mol×K Show Hide
S°liquid 213.10 J/mol×K NIST
S°liquid 214.70 J/mol×K NIST
Tboil [369.15; 373.35] K Show Hide
Tboil 372.65 K Measurement and correlation of binary vapor liquid equilibria of isomeric butanols with 1,4-dioxane
Tboil 372.34 K VLE of the binary systems (dimethyl carbonate with 2-propanol or 2-butanol) and (diethyl carbonate with methylcyclohexane) at 101.3 kPa
Tboil 372.35 K Isobaric (vapor + liquid) equilibrium data for the binary system methanol + 2-butyl alcohol and the quaternary system methyl acetate + methanol + 2-butyl alcohol + 2-butyl acetate at P = 101.33 kPa
Tboil 372.63 K Experimental isobaric vapour-liquid equilibrium data for the binary system (N, N-dimethyl acetamide + dimethyl sulfoxide) and the quaternary system (sec-butyl acetate + sec-butyl alcohol + N, N-dimethyl acetamide + dimethyl sulfoxide) at 101.3 kPa
Tboil 372.68 K Measurement and Correlation of Excess Molar Enthalpies for Ethylene Glycol + Alkanol Systems at the Temperatures (298.15, 308.15, and 323.15) K
Tboil 372.56 K Liquid-Liquid and Vapor-Liquid-Liquid Equilibrium of the 2-Butanone + 2-Butanol + Water System
Tboil 372.65 K Vapor-Liquid Equilibrium in the Binary Systems 2-Butanol + tert-Amyl Methyl Ether, 2-Butanol + Heptane, and Heptane + tert-Amyl Methyl Ether
Tboil 372.35 K Experimental Measurements of Vapor Liquid Equilibrium Data for the Binary Systems of Methanol + 2-Butyl Acetate, 2-Butyl Alcohol + 2-Butyl Acetate, and Methyl Acetate + 2-Butyl Acetate at 101.33 kPa
Tboil 372.76 K Experimental VLE data of Methyl Acetate or Ethyl Acetate with 2-Butanol at 0.3 and 0.6 MPa. Quality assessment and predictions.
Tboil 372.61 K Vapor-Liquid Equilibrium Behaviors of Vanillin in 1-Butanol, 2-Butanol, and 2-Methyl-1-propanol
Tboil 372.63 K Vapor Liquid Equilibrium Behaviors of 5-Methyl-2-(1-methylethyl)phenol in Alcohol
Tboil 372.66 K ChemSep v8.3 pure component data Compiled value
Tboil 372.66 K KDB
Tboil 372.66 K NCMS SOLV-DB
Tboil 372.66 ± 0.10 K NIST
Tboil 372.59 ± 0.25 K NIST
Tboil 373.00 K NIST
Tboil 372.62 ± 0.20 K NIST
Tboil 372.75 ± 0.30 K NIST
Tboil 372.70 K NIST
Tboil 372.40 ± 0.25 K NIST
Tboil 372.66 ± 0.15 K NIST
Tboil 372.70 ± 0.30 K NIST
Tboil 372.15 ± 0.40 K NIST
Tboil 372.90 ± 0.40 K NIST
Tboil 372.90 ± 0.30 K NIST
Tboil 372.90 ± 0.30 K NIST
Tboil 372.90 ± 0.30 K NIST
Tboil 372.70 ± 0.50 K NIST
Tboil 372.56 ± 0.12 K NIST
Tboil 372.65 K NIST
Tboil 372.85 ± 0.20 K NIST
Tboil 372.56 ± 0.10 K NIST
Tboil 371.40 ± 1.00 K NIST
Tboil 372.55 ± 0.30 K NIST
Tboil 371.65 ± 2.00 K NIST
Tboil Outlier 369.15 ± 3.00 K NIST
Tboil 372.15 ± 1.00 K NIST
Tboil 372.45 ± 0.30 K NIST
Tboil 372.55 ± 0.40 K NIST
Tboil 372.15 ± 1.00 K NIST
Tboil 371.40 ± 1.00 K NIST
Tboil 372.65 ± 0.50 K NIST
Tboil 372.65 ± 0.50 K NIST
Tboil 372.15 ± 0.50 K NIST
Tboil 372.65 ± 0.50 K NIST
Tboil 372.65 ± 0.50 K NIST
Tboil 372.65 ± 0.50 K NIST
Tboil 372.15 ± 1.00 K NIST
Tboil 372.70 ± 0.40 K NIST
Tboil 371.15 ± 1.00 K NIST
Tboil 372.20 ± 1.50 K NIST
Tboil 372.40 ± 0.50 K NIST
Tboil 373.35 ± 1.00 K NIST
Tboil 371.45 ± 0.50 K NIST
Tboil 372.40 ± 0.50 K NIST
Tboil 372.15 ± 2.00 K NIST
Tboil 373.15 ± 2.00 K NIST
Tboil 372.68 ± 0.10 K NIST
Tboil Outlier 370.90 ± 2.00 K NIST
Tboil 372.90 ± 0.50 K NIST
Tboil 372.75 ± 0.30 K NIST
Tboil 372.65 ± 0.30 K NIST
Tboil 372.00 ± 0.50 K NIST
Tboil 372.65 ± 0.30 K NIST
Tboil 372.65 ± 0.50 K NIST
Tboil 372.65 ± 0.10 K NIST
Tboil 372.35 ± 1.00 K NIST
Tboil 371.15 ± 1.00 K NIST
Tboil 373.15 ± 2.00 K NIST
Tboil 372.67 ± 0.20 K NIST
Tboil 372.65 ± 0.15 K NIST
Tboil 372.55 ± 0.10 K NIST
Tboil Outlier 370.65 ± 3.00 K NIST
Tboil 372.65 ± 0.05 K NIST
Tboil 372.68 ± 0.05 K NIST
Tboil 373.15 ± 1.00 K NIST
Tboil 371.85 ± 0.60 K NIST
Tboil 371.15 ± 1.00 K NIST
Tboil 372.65 ± 2.00 K NIST
Tboil 372.15 ± 2.00 K NIST
Tboil 372.15 ± 1.00 K NIST
Tboil 372.70 ± 0.50 K NIST
Tboil 372.40 ± 1.00 K NIST
Tboil 372.15 ± 1.00 K NIST
Tboil 371.65 ± 2.00 K NIST
Tboil 371.20 K NIST
Tboil 372.70 K NIST
Tc [535.95; 538.30] K Show Hide
Tc 536.29 K Experimental determination of critical data of multi-component mixtures containing potential gasoline additives 2-butanol by a flow-type apparatus
Tc 535.95 K Experimental study of the isochoric heat capacity and liquid-gas coexistence-curve properties of sec-butanol in the near- and supercritical regions
Tc 536.20 K IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Tc 536.00 K PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc 536.05 K ChemSep v8.3 pure component data Compiled value
Tc 536.20 K KDB
Tc 536.20 ± 0.30 K NIST
Tc 536.60 K NIST
Tc 536.10 ± 0.60 K NIST
Tc 536.10 ± 0.60 K NIST
Tc 536.18 K NIST
Tc 536.00 K NIST
Tc 535.98 K NIST
Tc Outlier 538.30 K NIST
Tfus [158.15; 158.45] K Show Hide
Tfus 158.15 K Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus 158.45 K ChemSep v8.3 pure component data Compiled value
Tfus 158.40 K KDB
Tfus 158.25 K Aq. Solubility Prediction
Tfus 158.45 K NCMS SOLV-DB
Tfus 158.45 K NIST
Ttriple [158.45; 184.73] K Show Hide
Ttriple 158.45 K ChemSep v8.3 pure component data Compiled value
Ttriple 184.73 ± 0.10 K NIST
Ttriple 184.70 ± 0.02 K NIST
Ttriple 184.70 ± 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 [0.268; 0.269] m3/kmol Show Hide
Vc 0.269 m3/kmol IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Vc 0.268 m3/kmol PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc 0.269 m3/kmol ChemSep v8.3 pure component data Compiled value
Vc 0.269 m3/kmol KDB
Vc 0.269 m3/kmol NIST
Zc [0.2520000; 0.2535390]   Show Hide
Zc 0.2530000 IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value
Zc 0.2520000 ChemSep v8.3 pure component data Compiled value
Zc 0.2535390 KDB
Zra 0.26 KDB

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,gas [131.71; 184.89] J/mol×K [365.15; 582.85] Show Hide
Cp,gas 131.71 ± 0.40 J/mol×K 365.15 NIST
Cp,gas 137.87 ± 0.67 J/mol×K 380.95 NIST
Cp,gas 136.52 ± 0.41 J/mol×K 383.15 NIST
Cp,gas 139.10 ± 0.67 J/mol×K 386.25 NIST
Cp,gas 140.85 ± 0.67 J/mol×K 393.75 NIST
Cp,gas 141.46 ± 0.42 J/mol×K 401.15 NIST
Cp,gas 143.50 ± 0.67 J/mol×K 405.15 NIST
Cp,gas 143.74 ± 0.67 J/mol×K 406.15 NIST
Cp,gas 146.32 ± 0.67 J/mol×K 417.25 NIST
Cp,gas 146.23 ± 0.44 J/mol×K 419.15 NIST
Cp,gas 150.96 ± 0.45 J/mol×K 437.15 NIST
Cp,gas 151.79 ± 0.67 J/mol×K 440.75 NIST
Cp,gas 155.64 ± 0.47 J/mol×K 455.15 NIST
Cp,gas 158.81 ± 0.67 J/mol×K 470.85 NIST
Cp,gas 169.31 ± 0.67 J/mol×K 515.95 NIST
Cp,gas 179.65 ± 0.67 J/mol×K 560.35 NIST
Cp,gas 184.89 ± 0.67 J/mol×K 582.85 NIST
Cp,liquid [184.90; 217.75] J/mol×K [281.70; 318.15] Show Hide
Cp,liquid 184.90 J/mol×K 281.70 NIST
Cp,liquid 186.96 J/mol×K 288.15 Thermodynamic Properties of dodecane + 1-butanol and + 2-butanol systems
Cp,liquid 199.20 J/mol×K 298.00 NIST
Cp,liquid 197.23 J/mol×K 298.15 Thermodynamic Properties of dodecane + 1-butanol and + 2-butanol systems
Cp,liquid 197.10 J/mol×K 298.15 NIST
Cp,liquid 198.03 J/mol×K 298.15 NIST
Cp,liquid 196.67 J/mol×K 298.15 NIST
Cp,liquid 197.40 J/mol×K 298.15 NIST
Cp,liquid 196.80 J/mol×K 298.15 NIST
Cp,liquid 207.51 J/mol×K 308.15 Thermodynamic Properties of dodecane + 1-butanol and + 2-butanol systems
Cp,liquid 217.75 J/mol×K 318.15 Thermodynamic Properties of dodecane + 1-butanol and + 2-butanol systems
η [0.0006218; 0.0049230] Pa×s [283.15; 353.15] Show Hide
η 0.0049230 Pa×s 283.15 Excess molar volume and viscosity study for the ternary system tetrahydrofuran (1) + 1-chlorobutane (2) + 2-butanol (3) at 283.15, 298.15 and 313.15 K
η 0.0045090 Pa×s 288.15 Densities and Viscosities of Binary Mixtures of 1-Bromobutane with Butanol Isomers at Several Temperatures
η 0.0045090 Pa×s 288.15 Densities and Viscosities of Binary Mixtures of 1-Chlorobutane with Butanol Isomers at Several Temperatures
η 0.0036250 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 0.0036250 Pa×s 293.15 Viscosities and Densities of Binary Mixtures of (N-Acetylmorpholine + Alkanols) from (293.15 to 323.15) K
η 0.0036230 Pa×s 293.15 Viscosities, Densities, and Speed of Sound of the Cycloalkanes with Secondary Alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO Interaction Parameters
η 0.0036630 Pa×s 293.15 Apparent Molar Volumes and Viscosities of Lauric, Palmitic, and Stearic Acids in 2-Butanol at (20, 30, 40, and 60) C
η 0.0042124 Pa×s 293.15 Molecular interactions in binary mixtures of formamide with 1-butanol, 2-butanol, 1,3-butanediol and 1,4-butanediol at different temperatures: An ultrasonic and viscometric study
η 0.0037438 Pa×s 293.15 Viscosities of binary mixtures containing 2-butanol + hydrocarbons (2,2,4-trimethylpentane or 1,2,4-trimethylbenzene) at high pressures for the implementation of second generation biofuels
η 0.0036230 Pa×s 293.15 Dynamic viscosities of 2-butanol with alkanes (C8, C10, and C12) at several temperatures
η 0.0036316 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 0.0036230 Pa×s 293.15 Viscosity, density, and speed of sound of methylcyclopentane with primary and secondary alcohols at T = (293.15, 298.15, and 303.15) K
η 0.0029950 Pa×s 298.15 Viscosities, Densities, and Speed of Sound of the Cycloalkanes with Secondary Alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO Interaction Parameters
η 0.0029975 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 0.0029950 Pa×s 298.15 Dynamic viscosities of 2-butanol with alkanes (C8, C10, and C12) at several temperatures
η 0.0030350 Pa×s 298.15 Densities and Viscosities of Binary Mixtures of 1-Bromobutane with Butanol Isomers at Several Temperatures
η 0.0030350 Pa×s 298.15 Densities and Viscosities of Binary Mixtures of 1-Chlorobutane with Butanol Isomers at Several Temperatures
η 0.0029980 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 0.0031050 Pa×s 298.15 Densities and viscosities of binary mixtures of ethylmethylketone and 2-alkanols; application of the ERAS model and cubic EOS
η 0.0030040 Pa×s 298.15 Excess molar volume and viscosity study for the ternary system tetrahydrofuran (1) + 1-chlorobutane (2) + 2-butanol (3) at 283.15, 298.15 and 313.15 K
η 0.0029950 Pa×s 298.15 Viscosity, density, and speed of sound of methylcyclopentane with primary and secondary alcohols at T = (293.15, 298.15, and 303.15) K
η 0.0029990 Pa×s 298.15 Densities, Viscosities, and Volumetric Properties of Binary Mixtures of 1,2-Propanediol + 1-Heptanol or 1-Hexanol and 1,2-Ethanediol + 2-Butanol or 2-Propanol at T = (298.15, 303.15, and 308.15) K
η 0.0029980 Pa×s 298.15 NCMS SOLV-DB
η 0.0030804 Pa×s 298.15 Measurements, Correlations, and Predictions of Viscosities for the Ternary Mixture (2-Butanol + Hexane + 1-Chlorobutane) at 298.15 K and 313.15 K
η 0.0030342 Pa×s 298.15 Molecular interactions in binary mixtures of formamide with 1-butanol, 2-butanol, 1,3-butanediol and 1,4-butanediol at different temperatures: An ultrasonic and viscometric study
η 0.0031040 Pa×s 298.15 Densities and Viscosities of Binary Mixtures of Cyclohexanone and 2-Alkanols
η 0.0025970 Pa×s 303.15 Densities and viscosities of binary mixtures of ethylmethylketone and 2-alkanols; application of the ERAS model and cubic EOS
η 0.0025270 Pa×s 303.15 Apparent Molar Volumes and Viscosities of Lauric, Palmitic, and Stearic Acids in 2-Butanol at (20, 30, 40, and 60) C
η 0.0024890 Pa×s 303.15 Viscosities and Densities of Binary Mixtures of (N-Acetylmorpholine + Alkanols) from (293.15 to 323.15) K
η 0.0024978 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 0.0024890 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 0.0024930 Pa×s 303.15 Viscosity, density, and speed of sound of methylcyclopentane with primary and secondary alcohols at T = (293.15, 298.15, and 303.15) K
η 0.0025970 Pa×s 303.15 Densities and Viscosities of Binary Mixtures of Cyclohexanone and 2-Alkanols
η 0.0024930 Pa×s 303.15 Dynamic viscosities of 2-butanol with alkanes (C8, C10, and C12) at several temperatures
η 0.0026066 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 0.0024990 Pa×s 303.15 Densities, Viscosities, and Volumetric Properties of Binary Mixtures of 1,2-Propanediol + 1-Heptanol or 1-Hexanol and 1,2-Ethanediol + 2-Butanol or 2-Propanol at T = (298.15, 303.15, and 308.15) K
η 0.0024930 Pa×s 303.15 Viscosities, Densities, and Speed of Sound of the Cycloalkanes with Secondary Alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO Interaction Parameters
η 0.0024954 Pa×s 303.15 Molecular interactions in binary mixtures of formamide with 1-butanol, 2-butanol, 1,3-butanediol and 1,4-butanediol at different temperatures: An ultrasonic and viscometric study
η 0.0020542 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 0.0024750 Pa×s 308.15 Densities, Viscosities, and Volumetric Properties of Binary Mixtures of 1,2-Propanediol + 1-Heptanol or 1-Hexanol and 1,2-Ethanediol + 2-Butanol or 2-Propanol at T = (298.15, 303.15, and 308.15) K
η 0.0021110 Pa×s 308.15 Densities and Viscosities of Binary Mixtures of 1-Bromobutane with Butanol Isomers at Several Temperatures
η 0.0021625 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 0.0021520 Pa×s 308.15 Densities and Viscosities of Binary Mixtures of Cyclohexanone and 2-Alkanols
η 0.0021058 Pa×s 308.15 Molecular interactions in binary mixtures of formamide with 1-butanol, 2-butanol, 1,3-butanediol and 1,4-butanediol at different temperatures: An ultrasonic and viscometric study
η 0.0021110 Pa×s 308.15 Densities and Viscosities of Binary Mixtures of 1-Chlorobutane with Butanol Isomers at Several Temperatures
η 0.0021530 Pa×s 308.15 Densities and viscosities of binary mixtures of ethylmethylketone and 2-alkanols; application of the ERAS model and cubic EOS
η 0.0017942 Pa×s 313.15 Measurements, Correlations, and Predictions of Viscosities for the Ternary Mixture (2-Butanol + Hexane + 1-Chlorobutane) at 298.15 K and 313.15 K
η 0.0017330 Pa×s 313.15 Densities and Viscosities of Binary Mixtures of Cyclohexanone and 2-Alkanols
η 0.0018010 Pa×s 313.15 Apparent Molar Volumes and Viscosities of Lauric, Palmitic, and Stearic Acids in 2-Butanol at (20, 30, 40, and 60) C
η 0.0018404 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 0.0017340 Pa×s 313.15 Densities and viscosities of binary mixtures of ethylmethylketone and 2-alkanols; application of the ERAS model and cubic EOS
η 0.0017880 Pa×s 313.15 Excess molar volume and viscosity study for the ternary system tetrahydrofuran (1) + 1-chlorobutane (2) + 2-butanol (3) at 283.15, 298.15 and 313.15 K
η 0.0017989 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 0.0020060 Pa×s 313.15 Viscosities and Densities of Binary Mixtures of (N-Acetylmorpholine + Alkanols) from (293.15 to 323.15) K
η 0.0017840 Pa×s 313.15 Molecular interactions in binary mixtures of formamide with 1-butanol, 2-butanol, 1,3-butanediol and 1,4-butanediol at different temperatures: An ultrasonic and viscometric study
η 0.0018324 Pa×s 313.15 Viscosities of binary mixtures containing 2-butanol + hydrocarbons (2,2,4-trimethylpentane or 1,2,4-trimethylbenzene) at high pressures for the implementation of second generation biofuels
η 0.0015242 Pa×s 318.15 Molecular interactions in binary mixtures of formamide with 1-butanol, 2-butanol, 1,3-butanediol and 1,4-butanediol at different temperatures: An ultrasonic and viscometric study
η 0.0015230 Pa×s 318.15 Densities and Viscosities of Binary Mixtures of 1-Chlorobutane with Butanol Isomers at Several Temperatures
η 0.0015230 Pa×s 318.15 Densities and Viscosities of Binary Mixtures of 1-Bromobutane with Butanol Isomers at Several Temperatures
η 0.0015570 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 0.0013327 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 0.0017170 Pa×s 323.15 Viscosities and Densities of Binary Mixtures of (N-Acetylmorpholine + Alkanols) from (293.15 to 323.15) K
η 0.0011508 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 0.0010017 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 0.0010111 Pa×s 333.15 Viscosities of binary mixtures containing 2-butanol + hydrocarbons (2,2,4-trimethylpentane or 1,2,4-trimethylbenzene) at high pressures for the implementation of second generation biofuels
η 0.0010250 Pa×s 333.15 Apparent Molar Volumes and Viscosities of Lauric, Palmitic, and Stearic Acids in 2-Butanol at (20, 30, 40, and 60) C
η 0.0008779 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 0.0007769 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
η 0.0006218 Pa×s 353.15 Viscosities of binary mixtures containing 2-butanol + hydrocarbons (2,2,4-trimethylpentane or 1,2,4-trimethylbenzene) at high pressures for the implementation of second generation biofuels
εr [14.94; 18.47]   [288.15; 308.15] Show Hide
εr 18.47 288.15 Static Permittivities of Isomeric Butanol Mixtures at Temperatures from (288.15 to 308.15) K
εr 17.51 293.15 Static Permittivities of Isomeric Butanol Mixtures at Temperatures from (288.15 to 308.15) K
εr 17.60 298.00 Dielectric constant of dimethyl sulfoxide - monohydric alcohol mixture solution at the microwave frequency
εr 16.60 298.15 Static Permittivities of Isomeric Butanol Mixtures at Temperatures from (288.15 to 308.15) K
εr 15.75 303.15 Static Permittivities of Isomeric Butanol Mixtures at Temperatures from (288.15 to 308.15) K
εr 14.94 308.15 Static Permittivities of Isomeric Butanol Mixtures at Temperatures from (288.15 to 308.15) K
ΔfusH [5.97; 6.00] kJ/mol [177.38; 184.70] Show Hide
ΔfusH 6.00 kJ/mol 177.38 NIST
ΔfusH 6.00 kJ/mol 177.38 NIST
ΔfusH 5.97 kJ/mol 184.70 NIST
ΔfusH 5.97 kJ/mol 184.70 NIST
ΔfusH 5.97 kJ/mol 184.70 NIST
ΔfusH 5.97 kJ/mol 184.70 NIST
ΔvapH [35.00; 57.50] kJ/mol [256.50; 506.00] Show Hide
ΔvapH 57.50 kJ/mol 256.50 NIST
ΔvapH 50.20 kJ/mol 297.00 NIST
ΔvapH 53.20 kJ/mol 336.50 NIST
ΔvapH 47.70 kJ/mol 339.50 NIST
ΔvapH 45.30 ± 0.10 kJ/mol 340.00 NIST
ΔvapH 47.80 kJ/mol 340.00 NIST
ΔvapH 48.80 kJ/mol 343.00 NIST
ΔvapH 44.10 kJ/mol 345.50 NIST
ΔvapH 48.10 kJ/mol 345.50 NIST
ΔvapH 46.30 kJ/mol 348.00 NIST
ΔvapH 46.20 kJ/mol 349.50 NIST
ΔvapH 49.30 kJ/mol 353.00 NIST
ΔvapH 43.30 ± 0.10 kJ/mol 355.00 NIST
ΔvapH 44.70 kJ/mol 359.50 NIST
ΔvapH 44.10 kJ/mol 363.00 NIST
ΔvapH 41.90 ± 0.10 kJ/mol 365.00 NIST
ΔvapH 43.20 kJ/mol 369.50 NIST
ΔvapH 43.20 kJ/mol 370.00 NIST
ΔvapH 40.80 ± 0.10 kJ/mol 372.00 NIST
ΔvapH 40.75 kJ/mol 372.70 NIST
ΔvapH 40.79 kJ/mol 372.80 KDB
ΔvapH 42.00 kJ/mol 386.00 NIST
ΔvapH 39.60 kJ/mol 440.00 NIST
ΔvapH 47.90 kJ/mol 448.00 NIST
ΔvapH 35.00 kJ/mol 506.00 NIST
ν [0.0000022; 0.0000037] m2/s [298.15; 313.15] Show Hide
ν 0.0000037 m2/s 298.15 Viscosities of Binary Mixtures of Isomeric Butanols or Isomeric Chlorobutanes with 2-Methyltetrahydrofuran
ν 0.0000022 m2/s 313.15 Viscosities of Binary Mixtures of Isomeric Butanols or Isomeric Chlorobutanes with 2-Methyltetrahydrofuran
Pvap [0.52; 2946.00] kPa [278.15; 513.15] Show Hide
Pvap 0.52 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 0.66 kPa 280.73 Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap 0.68 kPa 281.05 Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap 0.78 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 0.88 kPa 284.48 Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap 1.14 kPa 287.91 Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap 1.14 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 1.54 kPa 292.16 Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap 1.55 kPa 292.26 Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap 1.65 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 1.81 kPa 294.45 Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap 2.35 kPa 298.09 Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap 2.32 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 2.44 kPa 298.15 Vapor-Pressure Measurements of Liquid Solutions at Different Temperatures: Apparatus for Use over an Extended Temperature Range and Some New Data
Pvap 2.34 kPa 298.15 (Vapour + liquid) equilibrium and excess Gibbs functions of ternary mixtures containing 1-butanol or 2-butanol, n-hexane, and 1-chlorobutane at T = 298.15 K
Pvap 2.44 kPa 298.15 NCMS SOLV-DB
Pvap 2.85 kPa 301.02 Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap 3.26 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 3.37 kPa 303.15 Vapor-Pressure Measurements of Liquid Solutions at Different Temperatures: Apparatus for Use over an Extended Temperature Range and Some New Data
Pvap 3.41 kPa 303.90 Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap 4.46 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 4.47 kPa 308.15 Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap 4.59 kPa 308.15 Vapor-Pressure Measurements of Liquid Solutions at Different Temperatures: Apparatus for Use over an Extended Temperature Range and Some New Data
Pvap 5.51 kPa 311.60 Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap 5.97 kPa 313.10 Vapour liquid equilibrium for the 2-methylpropane + methanol, +ethanol, +2-propanol, +2-butanol and +2-methyl-2-propanol systems at 313.15K
Pvap 6.23 kPa 313.15 Vapor-Pressure Measurements of Liquid Solutions at Different Temperatures: Apparatus for Use over an Extended Temperature Range and Some New Data
Pvap 6.05 kPa 313.15 Isothermal vapor liquid equilibrium and molar excess Gibbs energies of two ternary systems containing either 1-butanol or 2-butanol + 1- hexene + methylbenzene at 313.15 K
Pvap 6.04 kPa 313.15 Phase equilibrium properties of binary and ternary mixtures containing 2-butanol, 2,2,4- trimethylpentane and 1-hexene at 313.15 K
Pvap 5.83 kPa 313.15 Vapor-Liquid Equilibria in Binary Systems Formed by n-Hexane with Alcohols
Pvap 6.05 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 6.55 kPa 314.41 Vapor Pressure and Its Temperature Dependence of 28 Organic Compounds: Cyclic Amines, Cyclic Ethers, and Cyclic and Open Chain Secondary Alcohols
Pvap 6.08 kPa 314.47 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 6.43 kPa 315.36 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 6.81 kPa 316.21 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 7.45 kPa 317.61 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 8.25 kPa 318.15 Vapor-Pressure Measurements of Liquid Solutions at Different Temperatures: Apparatus for Use over an Extended Temperature Range and Some New Data
Pvap 8.11 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 7.92 kPa 318.57 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 8.35 kPa 319.37 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 8.45 kPa 319.58 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 8.77 kPa 320.18 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 9.23 kPa 321.05 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 9.80 kPa 322.03 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 10.19 kPa 322.68 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 10.57 kPa 323.11 Isothermal Vapor Liquid Equilibrium for Binary 2-Methylpropene - C1-C4 Alcohol-Systems
Pvap 10.71 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 10.48 kPa 323.15 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 10.86 kPa 323.15 Vapor-Pressure Measurements of Liquid Solutions at Different Temperatures: Apparatus for Use over an Extended Temperature Range and Some New Data
Pvap 10.48 kPa 323.15 Vapor-Liquid Equilibria in Binary Systems Formed by n-Hexane with Alcohols
Pvap 10.70 kPa 323.17 Vapor Liquid Equilibrium for Butane + Methanol, + Ethanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-Propanol (TBA) at 323 K
Pvap 10.74 kPa 323.18 P-x data for binary systems using a novel static total pressure apparatus
Pvap 10.64 kPa 323.41 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 11.04 kPa 324.05 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 11.47 kPa 324.72 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 11.84 kPa 325.27 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 12.31 kPa 325.92 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 12.81 kPa 326.66 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 13.16 kPa 327.32 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 14.13 kPa 328.15 Vapor-Pressure Measurements of Liquid Solutions at Different Temperatures: Apparatus for Use over an Extended Temperature Range and Some New Data
Pvap 14.03 kPa 328.28 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 14.61 kPa 329.05 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 14.55 kPa 329.22 P-x data for binary systems using a novel static total pressure apparatus
Pvap 15.31 kPa 329.91 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 15.79 kPa 330.49 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 16.31 kPa 331.11 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 16.71 kPa 331.58 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 17.27 kPa 332.08 Vapor Liquid Equilibrium for the Trans-2-Butene + Methanol, + Ethanol, + 2-Propanol, + 2-Butanol and + 2-Methyl-2-Propanol Systems at 332 K
Pvap 17.25 kPa 332.17 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 17.87 kPa 332.81 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 18.34 kPa 333.15 Vapor-Pressure Measurements of Liquid Solutions at Different Temperatures: Apparatus for Use over an Extended Temperature Range and Some New Data
Pvap 18.20 kPa 333.15 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 18.20 kPa 333.15 Vapor-Liquid Equilibria in Binary Systems Formed by n-Hexane with Alcohols
Pvap 18.33 kPa 333.28 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 18.68 kPa 333.65 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 19.24 kPa 334.23 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 19.71 kPa 334.69 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 20.20 kPa 335.19 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 20.71 kPa 335.69 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 21.33 kPa 336.28 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 21.85 kPa 336.77 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 22.35 kPa 337.23 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 22.87 kPa 337.72 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 23.28 kPa 338.08 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 23.49 kPa 338.15 Vapor-Pressure Measurements of Liquid Solutions at Different Temperatures: Apparatus for Use over an Extended Temperature Range and Some New Data
Pvap 23.87 kPa 338.60 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 24.43 kPa 339.07 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 24.95 kPa 339.50 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 25.43 kPa 339.90 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 25.97 kPa 340.34 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 26.79 kPa 340.95 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 27.36 kPa 341.40 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 27.99 kPa 341.87 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 28.63 kPa 342.34 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 28.43 kPa 342.83 P-x data for binary systems using a novel static total pressure apparatus
Pvap 29.37 kPa 342.89 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 29.71 kPa 343.15 Vapor-Pressure Measurements of Liquid Solutions at Different Temperatures: Apparatus for Use over an Extended Temperature Range and Some New Data
Pvap 29.76 kPa 343.15 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 29.97 kPa 343.32 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 30.67 kPa 343.81 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 31.31 kPa 344.25 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 31.99 kPa 344.71 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 32.63 kPa 345.14 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 33.33 kPa 345.60 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 33.99 kPa 346.02 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 34.67 kPa 346.45 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 35.32 kPa 346.86 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 36.01 kPa 347.28 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 36.63 kPa 347.65 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 37.31 kPa 348.06 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 37.20 kPa 348.15 Vapor-Pressure Measurements of Liquid Solutions at Different Temperatures: Apparatus for Use over an Extended Temperature Range and Some New Data
Pvap 37.99 kPa 348.45 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 38.64 kPa 348.85 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 39.29 kPa 349.21 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 39.95 kPa 349.58 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 40.00 kPa 349.73 Isobaric Vapor-Liquid Equilibria for Tetrahydropyran and Alcohol Systems
Pvap 40.97 kPa 350.15 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 42.05 kPa 350.75 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 43.03 kPa 351.25 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 43.96 kPa 351.74 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 44.97 kPa 352.26 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 44.66 kPa 352.68 P-x data for binary systems using a novel static total pressure apparatus
Pvap 46.60 kPa 353.08 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 46.75 kPa 353.15 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 46.36 kPa 353.15 Vapor-Pressure Measurements of Liquid Solutions at Different Temperatures: Apparatus for Use over an Extended Temperature Range and Some New Data
Pvap 47.65 kPa 353.60 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 48.61 kPa 354.06 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 49.61 kPa 354.53 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 50.63 kPa 355.00 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 51.63 kPa 355.45 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 52.39 kPa 355.81 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 53.33 kPa 356.23 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 53.33 kPa 356.36 Isobaric Vapor-Liquid Equilibria for Tetrahydropyran and Alcohol Systems
Pvap 54.63 kPa 356.80 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 55.96 kPa 357.37 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 57.41 kPa 357.99 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 57.16 kPa 358.15 Vapor-Pressure Measurements of Liquid Solutions at Different Temperatures: Apparatus for Use over an Extended Temperature Range and Some New Data
Pvap 57.27 kPa 358.16 Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap 58.67 kPa 358.50 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 60.03 kPa 359.06 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 60.00 kPa 359.26 Isobaric Vapor Liquid Equilibria for the 2-Propanol + Ethylene Glycol Monopropyl Ether and 2-Butanol + Ethylene Glycol Monopropyl Ether Systems at 60 kPa, 80 kPa, and 100 kPa
Pvap 61.41 kPa 359.62 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 62.73 kPa 360.13 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 63.97 kPa 360.61 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 65.29 kPa 361.10 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 66.71 kPa 361.64 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 66.66 kPa 361.77 Isobaric Vapor-Liquid Equilibria for Tetrahydropyran and Alcohol Systems
Pvap 67.99 kPa 362.10 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 69.43 kPa 362.63 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 70.69 kPa 363.07 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 70.24 kPa 363.15 Vapor-Pressure Measurements of Liquid Solutions at Different Temperatures: Apparatus for Use over an Extended Temperature Range and Some New Data
Pvap 72.12 kPa 363.57 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 73.36 kPa 364.00 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 74.72 kPa 364.48 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 74.20 kPa 364.50 Vapour liquid equilibrium for the systems butane + methanol, +2-propanol, +1-butanol, +2-butanol, +2-methyl-2-propanol at 364.5K
Pvap 74.10 kPa 364.51 Vapor Liquid Equilibrium for the Systems 2-Methylpropane + Methanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-propanol at 364.5 K
Pvap 74.00 kPa 364.51 Isothermal Vapor Liquid Equilibrium for 2-Methylpropene + Methanol, + 1-Propanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-propanol Binary Systems at 364.5 K
Pvap 74.00 kPa 364.52 Vapor-Liquid Equilibrium for the cis-2-Butene + Methanol, + 2-Propanol, + 2-Butanol, + 2-Methyl-2-propanol Systems at 364.5 K
Pvap 75.40 kPa 364.52 Vapor Liquid Equilibrium for the Systems trans-2-Butene + Methanol, + 1-Propanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-propanol at 364.5 K
Pvap 76.00 kPa 364.90 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 77.31 kPa 365.33 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 78.65 kPa 365.76 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 79.95 kPa 366.18 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 79.99 kPa 366.36 Isobaric Vapor-Liquid Equilibria for Tetrahydropyran and Alcohol Systems
Pvap 80.00 kPa 366.45 Isobaric Vapor Liquid Equilibria for the 2-Propanol + Ethylene Glycol Monopropyl Ether and 2-Butanol + Ethylene Glycol Monopropyl Ether Systems at 60 kPa, 80 kPa, and 100 kPa
Pvap 81.35 kPa 366.63 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 82.63 kPa 367.04 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 84.03 kPa 367.47 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 85.39 kPa 367.88 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 84.94 kPa 367.97 Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap 85.16 kPa 367.97 Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap 86.71 kPa 368.27 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 88.05 kPa 368.68 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 89.41 kPa 369.08 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 90.67 kPa 369.43 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 91.91 kPa 369.79 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 93.33 kPa 370.19 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 93.32 kPa 370.38 Isobaric Vapor-Liquid Equilibria for Tetrahydropyran and Alcohol Systems
Pvap 94.44 kPa 370.56 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 96.00 kPa 370.94 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 97.35 kPa 371.32 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 98.59 kPa 371.65 Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 98.66 kPa 371.86 Isobaric Vapor-Liquid Equilibria for Tetrahydropyran and Alcohol Systems
Pvap 100.00 kPa 372.21 Isobaric Vapor Liquid Equilibria for the 2-Propanol + Ethylene Glycol Monopropyl Ether and 2-Butanol + Ethylene Glycol Monopropyl Ether Systems at 60 kPa, 80 kPa, and 100 kPa
Pvap 100.57 kPa 372.30 Vapor-Liquid Equilibrium of Binary Mixtures Containing Isopropyl Acetate and Alkanols at 101.32 kPa
Pvap 101.33 kPa 372.35 Experimental Measurements of Vapor Liquid Equilibrium Data for the Binary Systems of Methanol + 2-Butyl Acetate, 2-Butyl Alcohol + 2-Butyl Acetate, and Methyl Acetate + 2-Butyl Acetate at 101.33 kPa
Pvap 100.62 kPa 372.43 Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap 101.88 kPa 372.71 Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
Pvap 125.86 kPa 378.60 Vapor-Liquid Equilibrium of Binary Mixtures Containing Isopropyl Acetate and Alkanols at 101.32 kPa
Pvap 101.06 kPa 381.25 Salt effect on vapor liquid equilibria for binary systems of propanol/CaCl2 and butanol/CaCl2
Pvap 151.03 kPa 383.89 Vapor-Liquid Equilibrium of Binary Mixtures Containing Isopropyl Acetate and Alkanols at 101.32 kPa
Pvap 176.20 kPa 388.59 Vapor-Liquid Equilibrium of Binary Mixtures Containing Isopropyl Acetate and Alkanols at 101.32 kPa
Pvap 201.37 kPa 392.79 Vapor-Liquid Equilibrium of Binary Mixtures Containing Isopropyl Acetate and Alkanols at 101.32 kPa
Pvap 226.54 kPa 396.69 Vapor-Liquid Equilibrium of Binary Mixtures Containing Isopropyl Acetate and Alkanols at 101.32 kPa
Pvap 251.71 kPa 400.09 Vapor-Liquid Equilibrium of Binary Mixtures Containing Isopropyl Acetate and Alkanols at 101.32 kPa
Pvap 1351.00 kPa 468.15 Isothermal Vapor-Liquid Equilibria for the n-Pentane + 1-Butanol and n-Pentane + 2-Butanol Systems near the Critical Region of the Mixtures
Pvap 1500.00 kPa 473.46 Measurement and modeling of high pressure VLE for methyl acetate or ethyl acetate with 2-butanol. Isobaric data at 1.5 MPa
Pvap 1791.00 kPa 483.15 Isothermal Vapor-Liquid Equilibria for the n-Pentane + 1-Butanol and n-Pentane + 2-Butanol Systems near the Critical Region of the Mixtures
Pvap 2329.00 kPa 498.15 Isothermal Vapor-Liquid Equilibria for the n-Pentane + 1-Butanol and n-Pentane + 2-Butanol Systems near the Critical Region of the Mixtures
Pvap 2946.00 kPa 513.15 Isothermal Vapor-Liquid Equilibria for the n-Pentane + 1-Butanol and n-Pentane + 2-Butanol Systems near the Critical Region of the Mixtures
n0 [1.38352; 1.39951]   [288.15; 323.15] Show Hide
n0 1.39951 288.15 Experimental Determination and Modeling of Densities, Refractive Indices of the Binary Mixtures of Dimethylphthalate (or Dimethyladipate) + 1-Butanol, or + 2-Butanol, or + 2-Butanone at T = (288.15 to 323.15) K
n0 1.39951 288.15 Experimental Determination and Modeling of Densities and Refractive Indices of the Binary Systems Alcohol + Dicyclohexylamine at T = (288.15 to 323.15) K
n0 1.39730 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 1.39736 293.15 Experimental Determination and Modeling of Densities, Refractive Indices of the Binary Mixtures of Dimethylphthalate (or Dimethyladipate) + 1-Butanol, or + 2-Butanol, or + 2-Butanone at T = (288.15 to 323.15) K
n0 1.39430 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 1.39620 293.15 Measurement and correlation of the mutual solubility of diisopropylamine + water and triethylamine + water systems at high pressure
n0 1.39920 293.15 Relative Permittivities, Refractive Indices, and Densities of Dihydrofuran-2(3H)-one + Butan-1-ol and + Butan-2-ol at T = (293.15, 298.15, 303.15, and 313.15) K
n0 1.39780 293.15 Isothermal vapour-liquid equilibrium data for the binary systems 2-propanone + (2-butanol or propanoic acid)
n0 1.39720 293.15 Refractive Indices and Deviations in Refractive Indices for Binary Mixtures of Formamide + 1-Butanol, + 2-Butanol, + 1,3-Butanediol, and + 1,4-Butanediol at Temperatures from (293.15 to 318.15) K
n0 1.39736 293.15 Experimental Determination and Modeling of Densities and Refractive Indices of the Binary Systems Alcohol + Dicyclohexylamine at T = (288.15 to 323.15) K
n0 1.39760 293.15 Isothermal Vapor-Liquid Equilibrium Measurements for Alcohol + Water/n-Hexane Azeotropic Systems Using Both Dynamic and Automated Static-Synthetic Methods
n0 1.39550 293.15 Measurement and Correlation of the Solubilities of m-Phthalic Acid in Monobasic Alcohols
n0 1.39660 293.15 Densities, viscosities, excess molar volumes, and refractive indices of acetonitrile and 2-alkanols binary mixtures at different temperatures: Experimental results and application of the Prigogine Flory Patterson theory
n0 1.39830 293.15 Experimental solubility for betulin and estrone in various solvents within the temperature range T = (293.2 to 328.2) K
n0 1.39850 295.15 Isobaric Vapor Liquid Equilibrium Data for Binary Mixtures of 1-Phenylethanone with a Few Alcohols at 95.2 kPa
n0 1.39487 298.15 Effect of the temperature on the physical properties of the pure ionic liquid 1-ethyl-3-methylimidazolium methylsulfate and characterization of its binary mixtures with alcohols
n0 1.39515 298.15 Experimental Determination and Modeling of Densities and Refractive Indices of the Binary Systems Alcohol + Dicyclohexylamine at T = (288.15 to 323.15) K
n0 1.39430 298.15 Application of the ERAS model to volumetric properties of binary mixtures of banana oil with primary and secondary alcohols (C1- C4) at different temperatures
n0 1.39510 298.15 sothermal and Isobaric Vapor-Liquid Equilibrium and Excess Molar Enthalpy of the Binary Mixtures of 2-Methoxy-2-methylpropane + 2-Methyl-2-butanol or + 2-Butanol
n0 1.39540 298.15 Relative Permittivities, Refractive Indices, and Densities of Dihydrofuran-2(3H)-one + Butan-1-ol and + Butan-2-ol at T = (293.15, 298.15, 303.15, and 313.15) K
n0 1.39460 298.15 Densities, Viscosities, and Refractive Indices of Binary Mixtures of Acetophenone and 2-Alkanols
n0 1.39460 298.15 Densities, viscosities, excess molar volumes, and refractive indices of acetonitrile and 2-alkanols binary mixtures at different temperatures: Experimental results and application of the Prigogine Flory Patterson theory
n0 1.39530 298.15 Dielectric Properties of Methanol Mixtures with Ethanol, Isomers of Propanol, and Butanol
n0 1.39500 298.15 NCMS SOLV-DB
n0 1.39540 298.15 Isobaric (vapour + liquid) equilibrium for N-methyl-2-pyrrolidone with branched alcohols
n0 1.39530 298.15 Excess Gibbs free energies of the binary mixtures of acetonitrile with butanols at 94.83 kPa
n0 1.39530 298.15 Activity coefficients of the binary mixtures of a-cresol or p-cresol with C l-C4 aliphatic alcohols near ambient pressure
n0 1.39510 298.15 Refractive Indices and Deviations in Refractive Indices for Binary Mixtures of Formamide + 1-Butanol, + 2-Butanol, + 1,3-Butanediol, and + 1,4-Butanediol at Temperatures from (293.15 to 318.15) K
n0 1.39530 298.15 (Vapor + liquid) equilibria of the binary mixtures of m-cresol with C1 C4 aliphatic alcohols at 95.5 kPa
n0 1.39490 298.15 Isobaric (vapor+liquid) equilibrium for n-propyl acetate with 1-butanol or 2-butanol. Binary mixtures at 0.15 and 0.6 MPa
n0 1.39510 298.15 Vapor Liquid Equilibria, Excess Enthalpy, and Excess Volume of Binary Mixtures Containing an Alcohol (1-Butanol, 2-Butanol, or 2-Methyl-2-butanol) and 2-Ethoxy-2-methylbutane
n0 1.39676 298.15 Experimental determination and theoretical modeling of the vapor liquid equilibrium and densities of the binary system butan-2-ol + tetrahydro-2H-pyran
n0 1.39519 298.15 Isobaric vapour liquid equilibria for the binary systems 4-methyl-2-pentanone + 1-butanol and + 2-butanol at 20 and 101.3 kPa
n0 1.39540 298.15 Excess volumes and excess enthalpies of N-methyl-2-pyrrolidone with branched alcohols
n0 1.39515 298.15 Experimental Determination and Modeling of Densities, Refractive Indices of the Binary Mixtures of Dimethylphthalate (or Dimethyladipate) + 1-Butanol, or + 2-Butanol, or + 2-Butanone at T = (288.15 to 323.15) K
n0 1.39490 298.15 Liquid-Liquid and Vapor-Liquid-Liquid Equilibrium of the 4-Methyl-2-pentanone + 2-Butanol + Water System
n0 1.39530 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 1.39830 298.15 Bubble Temperatures of the Binary Mixtures of Dimethylcarbonate with Some Alcohols at 95.8 kPa
n0 1.39530 298.15 Excess Gibbs energies of selected binary mixtures formed by N,N-dimethyl formamide at 95.5 kPa
n0 1.39490 298.20 Ternary equilibrium data of mixtures consisting of 2-butanol, water, and heavy alcohols at T = 298.2 K
n0 1.39490 298.20 Relative permittivity data of binary mixtures containing 2-butanol, 2-butanone, and cyclohexane
n0 1.39240 303.15 Densities, viscosities, excess molar volumes, and refractive indices of acetonitrile and 2-alkanols binary mixtures at different temperatures: Experimental results and application of the Prigogine Flory Patterson theory
n0 1.39293 303.15 Experimental Determination and Modeling of Densities, Refractive Indices of the Binary Mixtures of Dimethylphthalate (or Dimethyladipate) + 1-Butanol, or + 2-Butanol, or + 2-Butanone at T = (288.15 to 323.15) K
n0 1.39480 303.15 Relative Permittivities, Refractive Indices, and Densities of Dihydrofuran-2(3H)-one + Butan-1-ol and + Butan-2-ol at T = (293.15, 298.15, 303.15, and 313.15) K
n0 1.39400 303.15 Experimental study on the calorimetric data of cyclohexanol with alkanols (C1-C4) and correlation with Wilson, NRTL and UNIQUAC models at 300 K
n0 1.39293 303.15 Experimental Determination and Modeling of Densities and Refractive Indices of the Binary Systems Alcohol + Dicyclohexylamine at T = (288.15 to 323.15) K
n0 1.39310 303.15 Refractive Indices and Deviations in Refractive Indices for Binary Mixtures of Formamide + 1-Butanol, + 2-Butanol, + 1,3-Butanediol, and + 1,4-Butanediol at Temperatures from (293.15 to 318.15) K
n0 1.39110 308.15 Refractive Indices and Deviations in Refractive Indices for Binary Mixtures of Formamide + 1-Butanol, + 2-Butanol, + 1,3-Butanediol, and + 1,4-Butanediol at Temperatures from (293.15 to 318.15) K
n0 1.39064 308.15 Experimental Determination and Modeling of Densities, Refractive Indices of the Binary Mixtures of Dimethylphthalate (or Dimethyladipate) + 1-Butanol, or + 2-Butanol, or + 2-Butanone at T = (288.15 to 323.15) K
n0 1.39064 308.15 Experimental Determination and Modeling of Densities and Refractive Indices of the Binary Systems Alcohol + Dicyclohexylamine at T = (288.15 to 323.15) K
n0 1.39050 308.15 Densities, viscosities, excess molar volumes, and refractive indices of acetonitrile and 2-alkanols binary mixtures at different temperatures: Experimental results and application of the Prigogine Flory Patterson theory
n0 1.39010 308.20 Relative permittivity data of binary mixtures containing 2-butanol, 2-butanone, and cyclohexane
n0 1.38910 313.15 Refractive Indices and Deviations in Refractive Indices for Binary Mixtures of Formamide + 1-Butanol, + 2-Butanol, + 1,3-Butanediol, and + 1,4-Butanediol at Temperatures from (293.15 to 318.15) K
n0 1.38832 313.15 Experimental Determination and Modeling of Densities, Refractive Indices of the Binary Mixtures of Dimethylphthalate (or Dimethyladipate) + 1-Butanol, or + 2-Butanol, or + 2-Butanone at T = (288.15 to 323.15) K
n0 1.38832 313.15 Experimental Determination and Modeling of Densities and Refractive Indices of the Binary Systems Alcohol + Dicyclohexylamine at T = (288.15 to 323.15) K
n0 1.39100 313.15 Relative Permittivities, Refractive Indices, and Densities of Dihydrofuran-2(3H)-one + Butan-1-ol and + Butan-2-ol at T = (293.15, 298.15, 303.15, and 313.15) K
n0 1.38710 318.15 Refractive Indices and Deviations in Refractive Indices for Binary Mixtures of Formamide + 1-Butanol, + 2-Butanol, + 1,3-Butanediol, and + 1,4-Butanediol at Temperatures from (293.15 to 318.15) K
n0 1.38596 318.15 Experimental Determination and Modeling of Densities and Refractive Indices of the Binary Systems Alcohol + Dicyclohexylamine at T = (288.15 to 323.15) K
n0 1.38596 318.15 Experimental Determination and Modeling of Densities, Refractive Indices of the Binary Mixtures of Dimethylphthalate (or Dimethyladipate) + 1-Butanol, or + 2-Butanol, or + 2-Butanone at T = (288.15 to 323.15) K
n0 1.38540 318.20 Relative permittivity data of binary mixtures containing 2-butanol, 2-butanone, and cyclohexane
n0 1.38352 323.15 Experimental Determination and Modeling of Densities, Refractive Indices of the Binary Mixtures of Dimethylphthalate (or Dimethyladipate) + 1-Butanol, or + 2-Butanol, or + 2-Butanone at T = (288.15 to 323.15) K
n0 1.38352 323.15 Experimental Determination and Modeling of Densities and Refractive Indices of the Binary Systems Alcohol + Dicyclohexylamine at T = (288.15 to 323.15) K
ρl [760.96; 815.39] kg/m3 [283.15; 343.15] Show Hide
ρl 815.39 kg/m3 283.15 Effects of alkyl group and temperature on the interactions between furfural and alcohol: Insight from density and sound velocity studies
ρl 814.99 kg/m3 283.15 Thermophysical study of the binary mixtures of N,N-dimethylacetamide with 2-propanol and 2-butanol
ρl 810.88 kg/m3 288.15 Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
ρl 810.52 kg/m3 288.15 Densities, Refractive Indices, Viscosities, and Spectroscopic Study of 1-Amino-2-propanol + 1-Butanol and + 2-Butanol Solutions at (288.15 to 333.15) K
ρl 810.69 kg/m3 288.15 Densities and Excess Molar Volumes of 2-Butanol + Cyclohexanamine + Heptane and 2-Butanol + n-Heptane at Temperatures between (288.15 and 323.15) K
ρl 810.69 kg/m3 288.15 Influence of chain length and degree of branching of alcohol + chlorobenzene mixtures on determination and modelling of VE by CEOS and CEOS/GE mixing rules
ρl 810.64 kg/m3 288.15 Densities and Excess Molar Volumes of the Ternary Mixture 2-Butanol + Chloroform + Benzene and Binary Mixtures 2-Butanol + Chloroform, or + Benzene over the Temperature Range (288.15 to 313.15) K
ρl 810.65 kg/m3 288.15 Volumetric and Viscometric Behavior of Binary Systems 2-Butanol + PEG 200, + PEG 400, + Tetraethylene Glycol Dimethyl Ether, and + N-Methyl-2-pyrrolidone
ρl 807.00 kg/m3 293.00 KDB
ρl 807.17 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 805.56 kg/m3 293.15 Densities and volumetric properties of (N-(2-hydroxyethyl)morpholine + ethanol, + 1-propanol, + 2-propanol, + 1-butanol, and + 2-butanol) at (293.15, 298.15, 303.15, 313.15, and 323.15) K
ρl 806.70 kg/m3 293.15 Studies on Thermodynamic and Transport Properties of Binary Mixtures Containing Alcohols and Aniline
ρl 806.95 kg/m3 293.15 Acoustic, volumetric and spectral studies of binary liquid mixtures of aliphatic dialkylamine and 2-alkanols at different temperatures
ρl 806.70 kg/m3 293.15 Influence of Temperature and Carbon Chain on Thermophysical Properties of Benzaldehyde/Alkan-2-ol Binary Mixtures
ρl 806.49 kg/m3 293.15 Densities, Refractive Indices, Viscosities, and Spectroscopic Study of 1-Amino-2-propanol + 1-Butanol and + 2-Butanol Solutions at (288.15 to 333.15) K
ρl 806.00 kg/m3 293.15 Density, speed of sound and refractive index of mixtures containing 2-phenoxyethanol with propanol or butanol at various temperatures
ρl 806.20 kg/m3 293.15 Density and Viscosity of 2-Butanol + (1-Propanol, 2-Propanol, or 3-Amino-1-propanol) Mixtures at Temperatures of (293.15 to 323.15) K: Application of the ERAS Model
ρl 807.19 kg/m3 293.15 Thermodynamic and spectroscopic interpretation of molecular interactions of nicotine + alcohol binary mixtures
ρl 806.84 kg/m3 293.15 Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
ρl 807.34 kg/m3 293.15 Effects of alkyl group and temperature on the interactions between furfural and alcohol: Insight from density and sound velocity studies
ρl 806.62 kg/m3 293.15 Volumetric and Viscometric Behavior of Binary Systems 2-Butanol + PEG 200, + PEG 400, + Tetraethylene Glycol Dimethyl Ether, and + N-Methyl-2-pyrrolidone
ρl 806.59 kg/m3 293.15 Densities and Excess Molar Volumes of the Ternary Mixture 2-Butanol + Chloroform + Benzene and Binary Mixtures 2-Butanol + Chloroform, or + Benzene over the Temperature Range (288.15 to 313.15) K
ρl 806.65 kg/m3 293.15 Influence of chain length and degree of branching of alcohol + chlorobenzene mixtures on determination and modelling of VE by CEOS and CEOS/GE mixing rules
ρl 806.56 kg/m3 293.15 Osmotic and apparent molar properties of binary mixtures alcohol + 1-butyl-3-methylimidazolium trifluoromethanesulfonate ionic liquid
ρl 806.70 kg/m3 293.15 Evaluation of thermodynamic properties of fluid mixtures by PC-SAFT model
ρl 806.70 kg/m3 293.15 Thermodynamic and transport properties of binary mixtures; friction theory coupled with PC-SAFT model
ρl 806.65 kg/m3 293.15 Densities and Excess Molar Volumes of 2-Butanol + Cyclohexanamine + Heptane and 2-Butanol + n-Heptane at Temperatures between (288.15 and 323.15) K
ρl 806.68 kg/m3 293.15 Molecular interactions in binary mixtures of 1-butoxy-2-propanol with alcohols at different temperatures: A thermophysical and spectroscopic approach
ρl 806.70 kg/m3 293.15 Densities and Viscosities of Binary Mixtures Containing Ethyl Formate and 2-Alkanols: Friction Theory and Free Volume Theory
ρl 802.70 kg/m3 298.15 Thermodynamic and transport properties of binary mixtures; friction theory coupled with PC-SAFT model
ρl 802.51 kg/m3 298.15 Experimental study on the calorimetric data of 2-butoxyethanol with aliphatic alcohols (C1-C4) and correlation with the Wilson, NRTL and UNIQUAC models at T = 298 K
ρl 803.09 kg/m3 298.15 Densities and viscosities of the mixtures (formamide + 2-alkanol): Experimental and theoretical approaches
ρl 802.56 kg/m3 298.15 Molecular interactions in binary mixtures of 1-butoxy-2-propanol with alcohols at different temperatures: A thermophysical and spectroscopic approach
ρl 802.70 kg/m3 298.15 Densities and Viscosities of Binary Mixtures Containing Ethyl Formate and 2-Alkanols: Friction Theory and Free Volume Theory
ρl 802.40 kg/m3 298.15 Densities, Ultrasonic Speeds, and Excess Properties of Binary Mixtures of Diethylene Glycol with 1-Butanol, 2-Butanol, and 1,4-Butanediol at Different Temperatures
ρl 803.00 kg/m3 298.15 Thermodynamic Properties of Binary Mixtures Containing N,N-Dimethylacetamide + 2-Alkanol: Experimental Data and Modeling
ρl 802.48 kg/m3 298.15 A combined experimental and computational investigation of excess molar enthalpies of (nitrobenzene + alkanol) mixtures
ρl 803.10 kg/m3 298.15 Measurement and Modeling of Volumetric Properties and Speeds of Sound of Several Mixtures of Alcohol Liquids Containing Butanediol
ρl 802.57 kg/m3 298.15 Liquid Liquid Equilibrium for Ternary Systems of Propyl Vinyl Ether + C3 or C4 Alcohols + Water at 298.15 K and Excess Molar Enthalpies for Ternary and Constituent Binary Systems of Propyl Vinyl Ether + Ethanol + Isooctane at 303.15 K
ρl 802.50 kg/m3 298.15 Volumetric and Viscometric Behavior of Binary Systems 2-Butanol + PEG 200, + PEG 400, + Tetraethylene Glycol Dimethyl Ether, and + N-Methyl-2-pyrrolidone
ρl 802.47 kg/m3 298.15 Densities and Excess Molar Volumes of the Ternary Mixture 2-Butanol + Chloroform + Benzene and Binary Mixtures 2-Butanol + Chloroform, or + Benzene over the Temperature Range (288.15 to 313.15) K
ρl 802.43 kg/m3 298.15 Densities and volumetric properties of (N-(2-hydroxyethyl)morpholine + ethanol, + 1-propanol, + 2-propanol, + 1-butanol, and + 2-butanol) at (293.15, 298.15, 303.15, 313.15, and 323.15) K
ρl 802.70 kg/m3 298.15 Evaluation of thermodynamic properties of fluid mixtures by PC-SAFT model
ρl 802.44 kg/m3 298.15 Surface Tensions of the Ternary Mixtures Containing an Isomeric Butanol + n-Hexane + 1-Chlorobutane at 298.15 K
ρl 802.40 kg/m3 298.15 Measurement and correlation of solubility and solution thermodynamics of 1,3-dimethylurea in different solvents from T = (288.15 to 328.15) K
ρl 802.40 kg/m3 298.15 Bubble point temperatures of the binary mixtures of nitrobenzene with C1 C4 aliphatic alcohols at 94.95 kPa
ρl 803.05 kg/m3 298.15 Thermodynamic and spectroscopic interpretation of molecular interactions of nicotine + alcohol binary mixtures
ρl 802.34 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 802.20 kg/m3 298.15 Experimental and predicted viscosities of the ternary mixture (hexane + 1,3-dioxolane + 2-butanol) at 298.15 and 313.15 K
ρl 802.40 kg/m3 298.15 Dynamic Viscosities of Diethyl Carbonate with Linear and Secondary Alcohols at Several Temperatures
ρl 802.00 kg/m3 298.15 Density and Viscosity of 2-Butanol + (1-Propanol, 2-Propanol, or 3-Amino-1-propanol) Mixtures at Temperatures of (293.15 to 323.15) K: Application of the ERAS Model
ρl 804.00 kg/m3 298.15 Liquid - liquid equilibrium for the quaternary reaction system water p sec-butyl alcohol p sec-butyl acetate p acetic acid
ρl 802.37 kg/m3 298.15 Densities, Refractive Indices, Viscosities, and Spectroscopic Study of 1-Amino-2-propanol + 1-Butanol and + 2-Butanol Solutions at (288.15 to 333.15) K
ρl 802.71 kg/m3 298.15 The study of physico-chemical properties of binary systems consisting of N-Methylcyclohexylamine with 2-alkanols at T = (298.15-328.15) K
ρl 802.40 kg/m3 298.15 Density, Speed of Sound, and Refractive Index Measurements for Binary Mixtures of Pentan-2-one with Propan-2-ol and Butan-2-ol
ρl 802.60 kg/m3 298.15 Isobaric Vapor-Liquid Equilibrium for the Binary Systems of 2-Butanol + 2-(Methoxymethoxy)-butane and 1-Butanol + 2-(Methoxymethoxy)-butane at 101.3 kPa
ρl 803.05 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 802.62 kg/m3 298.15 Excess molar volumes, viscosity deviations and excess thermal expansion coefficients for binary and ternary mixtures consist of diethylketone + 2-butanol + ethylchloroacetate at (298.15, 308.15 and 318.15) K
ρl 802.35 kg/m3 298.15 Measurements and correlation at different temperatures of liquid-liquid equilibria of 2-butanol or 2-methyl-2-butanol + 1,2,3-propanetriol + water ternary systems
ρl 802.47 kg/m3 298.15 Vapor-liquid equilibria of binary systems composed of polyoxyethylene 4-octylphenyl ether and alcohols: Experimental measurements and correlation
ρl 802.70 kg/m3 298.15 Influence of Temperature and Carbon Chain on Thermophysical Properties of Benzaldehyde/Alkan-2-ol Binary Mixtures
ρl 802.56 kg/m3 298.15 Thermodynamic and spectral investigations of binary liquid mixturesof 2-butoxy ethanol with alcohols at temperature range of 293.15-313.15 K
ρl 802.00 kg/m3 298.15 Density, speed of sound and refractive index of mixtures containing 2-phenoxyethanol with propanol or butanol at various temperatures
ρl 802.53 kg/m3 298.15 Densities and Excess Molar Volumes of 2-Butanol + Cyclohexanamine + Heptane and 2-Butanol + n-Heptane at Temperatures between (288.15 and 323.15) K
ρl 802.85 kg/m3 298.15 Acoustic, volumetric and spectral studies of binary liquid mixtures of aliphatic dialkylamine and 2-alkanols at different temperatures
ρl 802.70 kg/m3 298.15 Studies on Thermodynamic and Transport Properties of Binary Mixtures Containing Alcohols and Aniline
ρl 802.63 kg/m3 298.15 Liquid liquid equilibria for the binary system of di-isopropyl ether (DIPE) +water in between 288.15 and 323.15K and the ternary systems of DIPE +water + C1 C4 alcohols at 298.15K
ρl 802.88 kg/m3 298.15 Excess volumes and partial molar volumes of binary liquid mixtures of furfural or 2-methylfuran with alcohols at 298.15 K
ρl 802.71 kg/m3 298.15 Thermophysical study of the binary mixtures of N,N-dimethylacetamide with 2-propanol and 2-butanol
ρl 802.00 kg/m3 298.15 Binary Liquid-Liquid Equilibrium (LLE) for Dibutyl Ether (DBE) + Water from (288.15 to 318.15) K and Ternary LLE for Systems of DBE + C1 !less thanless than C4 Alcohols + Water at 298.15 K
ρl 802.73 kg/m3 298.15 Binary Liquid-Liquid Equilibrium (LLE) for Methyl tert-Amyl Ether (TAME) + Water from (288.15 to 313.15) K and Ternary LLE for Systems of TAME + C1-C4 Alcohols + Water at 298.15 K
ρl 802.72 kg/m3 298.15 Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
ρl 803.10 kg/m3 298.15 Apparent Molal Volumes and Viscosity B-Coefficients of Acetyl Salicylic Acid (2-Acetoxy Benzoic Acid) Solutions in Higher Alcohols at Different Temperatures
ρl 802.53 kg/m3 298.15 Influence of chain length and degree of branching of alcohol + chlorobenzene mixtures on determination and modelling of VE by CEOS and CEOS/GE mixing rules
ρl 802.36 kg/m3 298.20 Liquid-liquid equilibrium data for ternary systems of water + lactic acid + C4-C7 alcohols at 298.2 K and atmospheric pressure
ρl 802.49 kg/m3 298.20 Liquid-liquid equilibrium in systems used for the production of 5-hydroxymethylfurfural from biomass using alcohols as solvents
ρl 801.70 kg/m3 298.40 Vapor Liquid Equilibrium at 350 K, Excess Molar Enthalpies at 298 K, and Excess Molar Volumes at 298 K of Binary Mixtures Containing Ethyl Acetate, Butyl Acetate, and 2-Butanol
ρl 798.90 kg/m3 303.15 Thermodynamic Properties of Binary Mixtures Containing N,N-Dimethylacetamide + 2-Alkanol: Experimental Data and Modeling
ρl 799.20 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 798.85 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 798.40 kg/m3 303.15 Evaluation of thermodynamic properties of fluid mixtures by PC-SAFT model
ρl 797.90 kg/m3 303.15 Density and Viscosity of 2-Butanol + (1-Propanol, 2-Propanol, or 3-Amino-1-propanol) Mixtures at Temperatures of (293.15 to 323.15) K: Application of the ERAS Model
ρl 798.33 kg/m3 303.15 Densities and Excess Molar Volumes of 2-Butanol + Cyclohexanamine + Heptane and 2-Butanol + n-Heptane at Temperatures between (288.15 and 323.15) K
ρl 798.27 kg/m3 303.15 Densities and Excess Molar Volumes of the Ternary Mixture 2-Butanol + Chloroform + Benzene and Binary Mixtures 2-Butanol + Chloroform, or + Benzene over the Temperature Range (288.15 to 313.15) K
ρl 797.76 kg/m3 303.15 Densities and volumetric properties of (N-(2-hydroxyethyl)morpholine + ethanol, + 1-propanol, + 2-propanol, + 1-butanol, and + 2-butanol) at (293.15, 298.15, 303.15, 313.15, and 323.15) K
ρl 798.40 kg/m3 303.15 Thermodynamic and transport properties of binary mixtures; friction theory coupled with PC-SAFT model
ρl 798.30 kg/m3 303.15 Volumetric and Viscometric Behavior of Binary Systems 2-Butanol + PEG 200, + PEG 400, + Tetraethylene Glycol Dimethyl Ether, and + N-Methyl-2-pyrrolidone
ρl 798.99 kg/m3 303.15 Effects of alkyl group and temperature on the interactions between furfural and alcohol: Insight from density and sound velocity studies
ρl 798.35 kg/m3 303.15 Molecular interactions in binary mixtures of 1-butoxy-2-propanol with alcohols at different temperatures: A thermophysical and spectroscopic approach
ρl 798.51 kg/m3 303.15 Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
ρl 798.40 kg/m3 303.15 Studies of viscosities of dilute solutions of alkylamines in non-electrolyte solvents III. Alkylamines in butanols 303.15K
ρl 798.89 kg/m3 303.15 Measurement and Modeling of Volumetric Properties and Speeds of Sound of Several Mixtures of Alcohol Liquids Containing Butanediol
ρl 798.17 kg/m3 303.15 Densities, Refractive Indices, Viscosities, and Spectroscopic Study of 1-Amino-2-propanol + 1-Butanol and + 2-Butanol Solutions at (288.15 to 333.15) K
ρl 798.65 kg/m3 303.15 Acoustic, volumetric and spectral studies of binary liquid mixtures of aliphatic dialkylamine and 2-alkanols at different temperatures
ρl 798.40 kg/m3 303.15 Studies on Thermodynamic and Transport Properties of Binary Mixtures Containing Alcohols and Aniline
ρl 798.30 kg/m3 303.15 Densities, Ultrasonic Speeds, and Excess Properties of Binary Mixtures of Diethylene Glycol with 1-Butanol, 2-Butanol, and 1,4-Butanediol at Different Temperatures
ρl 798.00 kg/m3 303.15 Density, speed of sound and refractive index of mixtures containing 2-phenoxyethanol with propanol or butanol at various temperatures
ρl 798.40 kg/m3 303.15 Densities and Viscosities of Binary Mixtures Containing Ethyl Formate and 2-Alkanols: Friction Theory and Free Volume Theory
ρl 798.89 kg/m3 303.15 Densities and viscosities of the mixtures (formamide + 2-alkanol): Experimental and theoretical approaches
ρl 799.30 kg/m3 303.15 Density, Viscosities, and Excess Properties for Binary Mixtures of Sulfolane + Alcohols and Sulfolane + Glycols at Different Temperatures
ρl 798.33 kg/m3 303.15 Influence of chain length and degree of branching of alcohol + chlorobenzene mixtures on determination and modelling of VE by CEOS and CEOS/GE mixing rules
ρl 798.40 kg/m3 303.15 Influence of Temperature and Carbon Chain on Thermophysical Properties of Benzaldehyde/Alkan-2-ol Binary Mixtures
ρl 798.83 kg/m3 303.15 Thermodynamic and spectroscopic interpretation of molecular interactions of nicotine + alcohol binary mixtures
ρl 794.52 kg/m3 308.15 Thermodynamic and spectroscopic interpretation of molecular interactions of nicotine + alcohol binary mixtures
ρl 794.10 kg/m3 308.15 Influence of Temperature and Carbon Chain on Thermophysical Properties of Benzaldehyde/Alkan-2-ol Binary Mixtures
ρl 793.88 kg/m3 308.15 Densities, Refractive Indices, Viscosities, and Spectroscopic Study of 1-Amino-2-propanol + 1-Butanol and + 2-Butanol Solutions at (288.15 to 333.15) K
ρl 794.10 kg/m3 308.15 Densities and Viscosities of Binary Mixtures Containing Ethyl Formate and 2-Alkanols: Friction Theory and Free Volume Theory
ρl 794.10 kg/m3 308.15 Studies on Thermodynamic and Transport Properties of Binary Mixtures Containing Alcohols and Aniline
ρl 794.36 kg/m3 308.15 Acoustic, volumetric and spectral studies of binary liquid mixtures of aliphatic dialkylamine and 2-alkanols at different temperatures
ρl 794.55 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 795.04 kg/m3 308.15 Densities and viscosities of the mixtures (formamide + 2-alkanol): Experimental and theoretical approaches
ρl 794.59 kg/m3 308.15 Measurement and Modeling of Volumetric Properties and Speeds of Sound of Several Mixtures of Alcohol Liquids Containing Butanediol
ρl 795.00 kg/m3 308.15 Thermodynamic Properties of Binary Mixtures Containing N,N-Dimethylacetamide + 2-Alkanol: Experimental Data and Modeling
ρl 794.06 kg/m3 308.15 Molecular interactions in binary mixtures of 1-butoxy-2-propanol with alcohols at different temperatures: A thermophysical and spectroscopic approach
ρl 794.00 kg/m3 308.15 Volumetric and Viscometric Behavior of Binary Systems 2-Butanol + PEG 200, + PEG 400, + Tetraethylene Glycol Dimethyl Ether, and + N-Methyl-2-pyrrolidone
ρl 794.22 kg/m3 308.15 Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
ρl 794.00 kg/m3 308.15 Osmotic and apparent molar properties of binary mixtures alcohol + 1-butyl-3-methylimidazolium trifluoromethanesulfonate ionic liquid
ρl 794.20 kg/m3 308.15 The study of physico-chemical properties of binary systems consisting of N-Methylcyclohexylamine with 2-alkanols at T = (298.15-328.15) K
ρl 793.86 kg/m3 308.15 Density, Speed of Sound, and Refractive Index Measurements for Binary Mixtures of Pentan-2-one with Propan-2-ol and Butan-2-ol
ρl 794.10 kg/m3 308.15 Thermodynamic and transport properties of binary mixtures; friction theory coupled with PC-SAFT model
ρl 794.20 kg/m3 308.15 Densities, Ultrasonic Speeds, and Excess Properties of Binary Mixtures of Diethylene Glycol with 1-Butanol, 2-Butanol, and 1,4-Butanediol at Different Temperatures
ρl 794.03 kg/m3 308.15 Densities and Excess Molar Volumes of 2-Butanol + Cyclohexanamine + Heptane and 2-Butanol + n-Heptane at Temperatures between (288.15 and 323.15) K
ρl 793.97 kg/m3 308.15 Densities and Excess Molar Volumes of the Ternary Mixture 2-Butanol + Chloroform + Benzene and Binary Mixtures 2-Butanol + Chloroform, or + Benzene over the Temperature Range (288.15 to 313.15) K
ρl 794.05 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 794.10 kg/m3 308.15 Evaluation of thermodynamic properties of fluid mixtures by PC-SAFT model
ρl 793.60 kg/m3 308.15 Density and Viscosity of 2-Butanol + (1-Propanol, 2-Propanol, or 3-Amino-1-propanol) Mixtures at Temperatures of (293.15 to 323.15) K: Application of the ERAS Model
ρl 794.13 kg/m3 308.15 Excess molar volumes, viscosity deviations and excess thermal expansion coefficients for binary and ternary mixtures consist of diethylketone + 2-butanol + ethylchloroacetate at (298.15, 308.15 and 318.15) K
ρl 794.03 kg/m3 308.15 Influence of chain length and degree of branching of alcohol + chlorobenzene mixtures on determination and modelling of VE by CEOS and CEOS/GE mixing rules
ρl 789.49 kg/m3 313.15 Densities, Refractive Indices, Viscosities, and Spectroscopic Study of 1-Amino-2-propanol + 1-Butanol and + 2-Butanol Solutions at (288.15 to 333.15) K
ρl 790.15 kg/m3 313.15 Densities and viscosities of the mixtures (formamide + 2-alkanol): Experimental and theoretical approaches
ρl 789.80 kg/m3 313.15 Evaluation of thermodynamic properties of fluid mixtures by PC-SAFT model
ρl 789.59 kg/m3 313.15 Densities and Excess Molar Volumes of the Ternary Mixture 2-Butanol + Chloroform + Benzene and Binary Mixtures 2-Butanol + Chloroform, or + Benzene over the Temperature Range (288.15 to 313.15) K
ρl 790.11 kg/m3 313.15 Densities and volumetric properties of (N-(2-hydroxyethyl)morpholine + ethanol, + 1-propanol, + 2-propanol, + 1-butanol, and + 2-butanol) at (293.15, 298.15, 303.15, 313.15, and 323.15) K
ρl 789.20 kg/m3 313.15 Density and Viscosity of 2-Butanol + (1-Propanol, 2-Propanol, or 3-Amino-1-propanol) Mixtures at Temperatures of (293.15 to 323.15) K: Application of the ERAS Model
ρl 789.83 kg/m3 313.15 Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
ρl 789.65 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 790.19 kg/m3 313.15 Measurement and Modeling of Volumetric Properties and Speeds of Sound of Several Mixtures of Alcohol Liquids Containing Butanediol
ρl 790.28 kg/m3 313.15 Effects of alkyl group and temperature on the interactions between furfural and alcohol: Insight from density and sound velocity studies
ρl 789.86 kg/m3 313.15 Thermophysical study of the binary mixtures of N,N-dimethylacetamide with 2-propanol and 2-butanol
ρl 789.80 kg/m3 313.15 Densities and Viscosities of Binary Mixtures Containing Ethyl Formate and 2-Alkanols: Friction Theory and Free Volume Theory
ρl 789.63 kg/m3 313.15 Densities and Excess Molar Volumes of 2-Butanol + Cyclohexanamine + Heptane and 2-Butanol + n-Heptane at Temperatures between (288.15 and 323.15) K
ρl 790.10 kg/m3 313.15 Densities, Ultrasonic Speeds, and Excess Properties of Binary Mixtures of Diethylene Glycol with 1-Butanol, 2-Butanol, and 1,4-Butanediol at Different Temperatures
ρl 789.80 kg/m3 313.15 Thermodynamic and transport properties of binary mixtures; friction theory coupled with PC-SAFT model
ρl 789.80 kg/m3 313.15 Studies on Thermodynamic and Transport Properties of Binary Mixtures Containing Alcohols and Aniline
ρl 789.63 kg/m3 313.15 Influence of chain length and degree of branching of alcohol + chlorobenzene mixtures on determination and modelling of VE by CEOS and CEOS/GE mixing rules
ρl 789.00 kg/m3 313.15 Experimental Phase Equilibrium for the Binary System of n-Pentane +2-Propanol Using a New Equilibrium Cell and the Static Total Pressure Method
ρl 790.70 kg/m3 313.15 Density, Viscosities, and Excess Properties for Binary Mixtures of Sulfolane + Alcohols and Sulfolane + Glycols at Different Temperatures
ρl 789.61 kg/m3 313.15 Volumetric and Viscometric Behavior of Binary Systems 2-Butanol + PEG 200, + PEG 400, + Tetraethylene Glycol Dimethyl Ether, and + N-Methyl-2-pyrrolidone
ρl 789.00 kg/m3 313.15 Density, speed of sound and refractive index of mixtures containing 2-phenoxyethanol with propanol or butanol at various temperatures
ρl 789.80 kg/m3 313.15 Influence of Temperature and Carbon Chain on Thermophysical Properties of Benzaldehyde/Alkan-2-ol Binary Mixtures
ρl 789.67 kg/m3 313.15 Molecular interactions in binary mixtures of 1-butoxy-2-propanol with alcohols at different temperatures: A thermophysical and spectroscopic approach
ρl 790.13 kg/m3 313.15 Thermodynamic and spectroscopic interpretation of molecular interactions of nicotine + alcohol binary mixtures
ρl 790.16 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 790.20 kg/m3 313.15 Thermodynamic Properties of Binary Mixtures Containing N,N-Dimethylacetamide + 2-Alkanol: Experimental Data and Modeling
ρl 785.20 kg/m3 318.15 Thermodynamic and transport properties of binary mixtures; friction theory coupled with PC-SAFT model
ρl 785.20 kg/m3 318.15 Studies on Thermodynamic and Transport Properties of Binary Mixtures Containing Alcohols and Aniline
ρl 785.20 kg/m3 318.15 Evaluation of thermodynamic properties of fluid mixtures by PC-SAFT model
ρl 784.70 kg/m3 318.15 Density and Viscosity of 2-Butanol + (1-Propanol, 2-Propanol, or 3-Amino-1-propanol) Mixtures at Temperatures of (293.15 to 323.15) K: Application of the ERAS Model
ρl 785.64 kg/m3 318.15 Thermodynamic and spectroscopic interpretation of molecular interactions of nicotine + alcohol binary mixtures
ρl 785.20 kg/m3 318.15 Influence of Temperature and Carbon Chain on Thermophysical Properties of Benzaldehyde/Alkan-2-ol Binary Mixtures
ρl 784.99 kg/m3 318.15 Densities, Refractive Indices, Viscosities, and Spectroscopic Study of 1-Amino-2-propanol + 1-Butanol and + 2-Butanol Solutions at (288.15 to 333.15) K
ρl 785.69 kg/m3 318.15 Measurement and Modeling of Volumetric Properties and Speeds of Sound of Several Mixtures of Alcohol Liquids Containing Butanediol
ρl 785.15 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 785.11 kg/m3 318.15 Volumetric and Viscometric Behavior of Binary Systems 2-Butanol + PEG 200, + PEG 400, + Tetraethylene Glycol Dimethyl Ether, and + N-Methyl-2-pyrrolidone
ρl 785.22 kg/m3 318.15 Excess molar volumes, viscosity deviations and excess thermal expansion coefficients for binary and ternary mixtures consist of diethylketone + 2-butanol + ethylchloroacetate at (298.15, 308.15 and 318.15) K
ρl 785.12 kg/m3 318.15 Densities and Excess Molar Volumes of 2-Butanol + Cyclohexanamine + Heptane and 2-Butanol + n-Heptane at Temperatures between (288.15 and 323.15) K
ρl 785.20 kg/m3 318.15 Densities and Viscosities of Binary Mixtures Containing Ethyl Formate and 2-Alkanols: Friction Theory and Free Volume Theory
ρl 785.26 kg/m3 318.15 Density, Speed of Sound, and Refractive Index Measurements for Binary Mixtures of Pentan-2-one with Propan-2-ol and Butan-2-ol
ρl 785.32 kg/m3 318.15 The study of physico-chemical properties of binary systems consisting of N-Methylcyclohexylamine with 2-alkanols at T = (298.15-328.15) K
ρl 785.66 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 780.55 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 780.38 kg/m3 323.15 Densities, Refractive Indices, Viscosities, and Spectroscopic Study of 1-Amino-2-propanol + 1-Butanol and + 2-Butanol Solutions at (288.15 to 333.15) K
ρl 780.60 kg/m3 323.15 Thermodynamic and transport properties of binary mixtures; friction theory coupled with PC-SAFT model
ρl 781.04 kg/m3 323.15 Thermodynamic and spectroscopic interpretation of molecular interactions of nicotine + alcohol binary mixtures
ρl 781.70 kg/m3 323.15 Density, Viscosities, and Excess Properties for Binary Mixtures of Sulfolane + Alcohols and Sulfolane + Glycols at Different Temperatures
ρl 780.60 kg/m3 323.15 Densities and Viscosities of Binary Mixtures Containing Ethyl Formate and 2-Alkanols: Friction Theory and Free Volume Theory
ρl 780.50 kg/m3 323.15 Osmotic and apparent molar properties of binary mixtures alcohol + 1-butyl-3-methylimidazolium trifluoromethanesulfonate ionic liquid
ρl 780.00 kg/m3 323.15 Density, speed of sound and refractive index of mixtures containing 2-phenoxyethanol with propanol or butanol at various temperatures
ρl 780.60 kg/m3 323.15 Studies on Thermodynamic and Transport Properties of Binary Mixtures Containing Alcohols and Aniline
ρl 780.40 kg/m3 323.15 Osmotic coefficients and apparent molar volumes of 1-hexyl-3-methylimidazolium trifluoromethanesulfonate ionic liquid in alcohols
ρl 780.50 kg/m3 323.15 Volumetric and Viscometric Behavior of Binary Systems 2-Butanol + PEG 200, + PEG 400, + Tetraethylene Glycol Dimethyl Ether, and + N-Methyl-2-pyrrolidone
ρl 781.09 kg/m3 323.15 Measurement and Modeling of Volumetric Properties and Speeds of Sound of Several Mixtures of Alcohol Liquids Containing Butanediol
ρl 780.60 kg/m3 323.15 Influence of Temperature and Carbon Chain on Thermophysical Properties of Benzaldehyde/Alkan-2-ol Binary Mixtures
ρl 784.92 kg/m3 323.15 Densities and volumetric properties of (N-(2-hydroxyethyl)morpholine + ethanol, + 1-propanol, + 2-propanol, + 1-butanol, and + 2-butanol) at (293.15, 298.15, 303.15, 313.15, and 323.15) K
ρl 780.51 kg/m3 323.15 Densities and Excess Molar Volumes of 2-Butanol + Cyclohexanamine + Heptane and 2-Butanol + n-Heptane at Temperatures between (288.15 and 323.15) K
ρl 780.60 kg/m3 323.15 Evaluation of thermodynamic properties of fluid mixtures by PC-SAFT model
ρl 781.05 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 780.20 kg/m3 323.15 Density and Viscosity of 2-Butanol + (1-Propanol, 2-Propanol, or 3-Amino-1-propanol) Mixtures at Temperatures of (293.15 to 323.15) K: Application of the ERAS Model
ρl 775.83 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 775.66 kg/m3 328.15 Densities, Refractive Indices, Viscosities, and Spectroscopic Study of 1-Amino-2-propanol + 1-Butanol and + 2-Butanol Solutions at (288.15 to 333.15) K
ρl 775.73 kg/m3 328.15 Density, Speed of Sound, and Refractive Index Measurements for Binary Mixtures of Pentan-2-one with Propan-2-ol and Butan-2-ol
ρl 776.34 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 775.52 kg/m3 328.15 The study of physico-chemical properties of binary systems consisting of N-Methylcyclohexylamine with 2-alkanols at T = (298.15-328.15) K
ρl 772.10 kg/m3 333.15 Density, Viscosities, and Excess Properties for Binary Mixtures of Sulfolane + Alcohols and Sulfolane + Glycols at Different Temperatures
ρl 770.82 kg/m3 333.15 Densities, Refractive Indices, Viscosities, and Spectroscopic Study of 1-Amino-2-propanol + 1-Butanol and + 2-Butanol Solutions at (288.15 to 333.15) K
ρl 770.99 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 771.51 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 766.03 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 765.75 kg/m3 338.15 Density, Speed of Sound, and Refractive Index Measurements for Binary Mixtures of Pentan-2-one with Propan-2-ol and Butan-2-ol
ρl 762.00 kg/m3 343.15 Density, Viscosities, and Excess Properties for Binary Mixtures of Sulfolane + Alcohols and Sulfolane + Glycols at Different Temperatures
ρl 760.96 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
ΔfusS [32.32; 33.83] J/mol×K [177.38; 184.70] Show Hide
ΔfusS 33.83 J/mol×K 177.38 NIST
ΔfusS 33.83 J/mol×K 177.38 NIST
ΔfusS 32.32 J/mol×K 184.70 NIST
ΔfusS 32.32 J/mol×K 184.70 NIST
csound,fluid [1120.30; 1266.60] m/s [283.15; 323.15] Show Hide
csound,fluid 1266.60 m/s 283.15 Excess Enthalpy, Density, and Speed of Sound for the Mixtures a-Pinene + 1-Butanol or 2-Butanol at (283.15, 298.15, and 313.15) K
csound,fluid 1229.50 m/s 293.15 Acoustic, volumetric and osmotic properties of binary mixtures containing the ionic liquid 1-butyl-3-methylimidazolim dicyanamide mixed with primary and secondary alcohols
csound,fluid 1212.40 m/s 298.15 Excess Enthalpy, Density, and Speed of Sound for the Mixtures a-Pinene + 1-Butanol or 2-Butanol at (283.15, 298.15, and 313.15) K
csound,fluid 1175.50 m/s 308.15 Acoustic, volumetric and osmotic properties of binary mixtures containing the ionic liquid 1-butyl-3-methylimidazolim dicyanamide mixed with primary and secondary alcohols
csound,fluid 1158.00 m/s 313.15 Excess Enthalpy, Density, and Speed of Sound for the Mixtures a-Pinene + 1-Butanol or 2-Butanol at (283.15, 298.15, and 313.15) K
csound,fluid 1120.30 m/s 323.15 Acoustic, volumetric and osmotic properties of binary mixtures containing the ionic liquid 1-butyl-3-methylimidazolim dicyanamide mixed with primary and secondary alcohols
γ [0.02; 0.02] N/m [283.15; 323.15] Show Hide
γ 0.02 N/m 283.15 Study of the Temperature Dependence of Surface Tensions of Some Alkanol + Hexane Mixtures
γ 0.02 N/m 288.15 Study of the Temperature Dependence of Surface Tensions of Some Alkanol + Hexane Mixtures
γ 0.02 N/m 293.15 Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol
γ 0.02 N/m 293.15 Study of the Temperature Dependence of Surface Tensions of Some Alkanol + Hexane Mixtures
γ 0.02 N/m 293.20 KDB
γ 0.02 N/m 298.15 Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol
γ 0.02 N/m 298.15 NCMS SOLV-DB
γ 0.02 N/m 298.15 Concentration Dependence of Surface Tension for Very Dilute Aqueous Solutions of Organic Non-Electrolytes
γ 0.02 N/m 298.15 Study of the Temperature Dependence of Surface Tensions of Some Alkanol + Hexane Mixtures
γ 0.02 N/m 303.15 Study of the Temperature Dependence of Surface Tensions of Some Alkanol + Hexane Mixtures
γ 0.02 N/m 303.15 Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol
γ 0.02 N/m 308.15 Study of the Temperature Dependence of Surface Tensions of Some Alkanol + Hexane Mixtures
γ 0.02 N/m 308.15 Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol
γ 0.02 N/m 313.15 Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol
γ 0.02 N/m 313.15 Study of the Temperature Dependence of Surface Tensions of Some Alkanol + Hexane Mixtures
γ 0.02 N/m 318.15 Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol
γ 0.02 N/m 323.15 Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol

Pressure Dependent Properties

Property Value Unit Pressure (kPa) Source
Tboil(P) [388.57; 430.17] K [174.70; 566.90] Show Hide
Tboil(P) 388.57 K 174.70 Isobaric Vapor-Liquid Equilibrium Measurements and Separation Process for the Quinary Methanol + Methylal + 2-Butanol + 2-(Methoxymethoxy)-butane + (+-)-Di-sec-butoxymethane System
Tboil(P) 399.33 K 244.60 Isobaric Vapor-Liquid Equilibrium Measurements and Separation Process for the Quinary Methanol + Methylal + 2-Butanol + 2-(Methoxymethoxy)-butane + (+-)-Di-sec-butoxymethane System
Tboil(P) 407.43 K 309.70 Isobaric Vapor-Liquid Equilibrium Measurements and Separation Process for the Quinary Methanol + Methylal + 2-Butanol + 2-(Methoxymethoxy)-butane + (+-)-Di-sec-butoxymethane System
Tboil(P) 419.33 K 429.60 Isobaric Vapor-Liquid Equilibrium Measurements and Separation Process for the Quinary Methanol + Methylal + 2-Butanol + 2-(Methoxymethoxy)-butane + (+-)-Di-sec-butoxymethane System
Tboil(P) 430.17 K 566.90 Isobaric Vapor-Liquid Equilibrium Measurements and Separation Process for the Quinary Methanol + Methylal + 2-Butanol + 2-(Methoxymethoxy)-butane + (+-)-Di-sec-butoxymethane System

Datasets

  1. Viscosity, Pa*s (1)
  2. Mass density, kg/m3 (7)
  3. Speed of sound, m/s (1)

Viscosity, Pa*s

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Viscosity, Pa*s - Liquid
298.15 81.50 0.0031
Reference

Mass density, kg/m3

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
313.14 1029.00 789.61
313.14 2044.00 790.47
313.14 3044.00 791.33
313.14 4020.00 792.13
313.14 5025.00 792.97
313.14 6034.00 793.81
313.14 7015.00 794.62
313.14 8047.00 795.46
313.14 9042.00 796.28
313.14 10036.00 797.07
313.14 11056.00 797.88
313.14 12015.00 798.62
313.14 12998.00 799.38
313.14 14031.00 800.18
313.14 15062.00 800.96
313.14 16045.00 801.69
313.14 17029.00 802.41
313.14 18032.00 803.15
313.14 19014.00 803.87
313.14 20007.00 804.59
313.14 21048.00 805.31
313.14 22005.00 806.01
313.14 23044.00 806.75
313.14 24040.00 807.45
313.14 25011.00 808.16
323.12 1024.00 780.71
323.12 2019.00 781.62
323.12 3028.00 782.53
323.12 4054.00 783.45
323.12 5025.00 784.31
323.12 6046.00 785.21
323.12 7009.00 786.05
323.12 8016.00 786.93
323.12 9036.00 787.81
323.12 10038.00 788.67
323.12 11085.00 789.54
323.12 12007.00 790.3
323.12 13058.00 791.16
323.12 14013.00 791.95
323.12 15014.00 792.76
323.12 16058.00 793.57
323.12 17014.00 794.33
323.12 18066.00 795.16
323.12 19017.00 795.87
323.12 20012.00 796.64
323.12 21035.00 797.41
323.12 22018.00 798.15
323.12 23008.00 798.89
323.12 24063.00 799.69
323.12 25023.00 800.41
333.03 1039.00 771.36
333.03 2067.00 772.38
333.03 3015.00 773.31
333.03 4021.00 774.28
333.03 5051.00 775.27
333.03 6077.00 776.24
333.03 7027.00 777.14
333.03 8030.00 778.08
333.03 9062.00 779.01
333.03 10008.00 779.89
333.03 11025.00 780.81
333.03 12015.00 781.69
333.03 13018.00 782.57
333.03 14014.00 783.42
333.03 15028.00 784.3
333.03 16021.00 785.13
333.03 16999.00 785.94
333.03 18050.00 786.8
333.03 19020.00 787.6
333.03 20010.00 788.39
333.03 21025.00 789.2
333.03 22010.00 789.98
333.03 23020.00 790.79
333.03 24018.00 791.59
333.03 25029.00 792.38
342.96 1035.00 761.81
342.96 2085.00 762.95
342.96 3051.00 763.94
342.96 4055.00 764.99
342.96 5022.00 765.98
342.96 6004.00 766.98
342.96 7054.00 768.04
342.96 8030.00 769.0
342.96 9030.00 769.98
342.96 10053.00 770.95
342.96 11019.00 771.86
342.96 12025.00 772.81
342.96 13011.00 773.71
342.96 14015.00 774.61
342.96 15006.00 775.48
342.96 16036.00 776.39
342.96 17036.00 777.26
342.96 18028.00 778.1
342.96 19010.00 778.91
342.96 20038.00 779.76
342.96 21011.00 780.56
342.96 22029.00 781.38
342.96 23030.00 782.18
342.96 24002.00 782.96
342.96 25033.00 783.79
352.86 1041.00 751.57
352.86 2041.00 752.74
352.86 3066.00 753.92
352.86 4033.00 755.01
352.86 5062.00 756.18
352.86 6051.00 757.26
352.86 7059.00 758.35
352.86 8019.00 759.39
352.86 9040.00 760.46
352.86 10062.00 761.53
352.86 11019.00 762.52
352.86 12023.00 763.54
352.86 13025.00 764.55
352.86 14025.00 765.53
352.86 15018.00 766.5
352.86 16019.00 767.48
352.86 17041.00 768.42
352.86 18025.00 769.37
352.86 19020.00 770.27
352.86 20020.00 771.19
352.86 21023.00 772.11
352.86 22008.00 772.97
352.86 23013.00 773.88
352.86 24029.00 774.79
352.86 25009.00 775.65
362.79 1034.00 740.13
362.79 2005.00 741.38
362.79 3035.00 742.67
362.79 3999.00 743.86
362.79 5056.00 745.14
362.79 6053.00 746.34
362.79 7031.00 747.5
362.79 8032.00 748.66
362.79 9052.00 749.84
362.79 10045.00 750.95
362.79 11009.00 752.02
362.79 12031.00 753.14
362.79 13018.00 754.21
362.79 14007.00 755.25
362.79 15026.00 756.31
362.79 15999.00 757.31
362.79 17038.00 758.37
362.79 18013.00 759.36
362.79 18998.00 760.34
362.79 20016.00 761.31
362.79 21005.00 762.29
362.79 22009.00 763.23
362.79 23012.00 764.19
362.79 24007.00 765.14
362.79 25037.00 766.09
Reference
Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
293.15 100.00 806.7
293.15 1000.00 807.4
293.15 5000.00 810.4
293.15 10000.00 814.0
293.15 15000.00 817.4
293.15 20000.00 820.7
293.15 25000.00 823.9
293.15 30000.00 826.9
293.15 35000.00 829.9
293.15 40000.00 832.7
293.15 45000.00 835.4
293.15 50000.00 838.1
293.15 55000.00 840.6
293.15 60000.00 843.2
293.15 65000.00 845.7
293.15 70000.00 848.0
293.15 80000.00 852.6
293.15 90000.00 857.1
293.15 100000.00 861.2
293.15 110000.00 865.3
293.15 120000.00 869.2
293.15 130000.00 873.0
293.15 140000.00 876.6
298.15 100.00 802.6
298.15 1000.00 803.3
298.15 5000.00 806.4
298.15 10000.00 810.1
298.15 15000.00 813.6
298.15 20000.00 817.0
298.15 25000.00 820.2
298.15 30000.00 823.4
298.15 35000.00 826.3
298.15 40000.00 829.2
298.15 45000.00 832.0
298.15 50000.00 834.7
298.15 55000.00 837.4
298.15 60000.00 839.9
298.15 65000.00 842.4
298.15 70000.00 844.8
298.15 80000.00 849.5
298.15 90000.00 854.0
298.15 100000.00 858.2
298.15 110000.00 862.4
298.15 120000.00 866.2
298.15 130000.00 870.1
298.15 140000.00 873.7
313.15 100.00 789.5
313.15 1000.00 790.3
313.15 5000.00 793.6
313.15 10000.00 797.7
313.15 15000.00 801.6
313.15 20000.00 805.2
313.15 25000.00 808.5
313.15 30000.00 812.1
313.15 35000.00 815.3
313.15 40000.00 818.4
313.15 45000.00 821.3
313.15 50000.00 824.2
313.15 55000.00 827.0
313.15 60000.00 829.8
313.15 65000.00 832.5
313.15 70000.00 835.0
313.15 80000.00 839.9
313.15 90000.00 844.7
313.15 100000.00 849.1
313.15 110000.00 853.4
313.15 120000.00 857.5
313.15 130000.00 861.5
313.15 140000.00 865.4
333.15 100.00 770.8
333.15 1000.00 771.7
333.15 5000.00 775.6
333.15 10000.00 780.2
333.15 15000.00 784.6
333.15 20000.00 788.8
333.15 25000.00 792.6
333.15 30000.00 796.3
333.15 35000.00 800.0
333.15 40000.00 803.4
333.15 45000.00 806.6
333.15 50000.00 809.7
333.15 55000.00 812.8
333.15 60000.00 815.8
333.15 65000.00 818.7
333.15 70000.00 821.4
333.15 80000.00 826.7
333.15 90000.00 831.9
333.15 100000.00 836.7
333.15 110000.00 841.2
333.15 120000.00 845.5
333.15 130000.00 849.8
333.15 140000.00 853.8
353.21 100.00 750.3
353.21 1000.00 751.4
353.21 5000.00 756.0
353.21 10000.00 761.3
353.21 15000.00 766.4
353.21 20000.00 771.0
353.21 25000.00 775.4
353.21 30000.00 779.5
353.21 35000.00 783.5
353.21 40000.00 787.2
353.21 45000.00 790.8
353.21 50000.00 794.5
353.21 55000.00 797.7
353.21 60000.00 801.0
353.21 65000.00 804.1
353.21 70000.00 807.2
353.21 80000.00 812.9
353.21 90000.00 818.3
353.21 100000.00 823.5
353.21 110000.00 828.5
353.21 120000.00 833.1
353.21 130000.00 837.6
353.21 140000.00 842.0
373.24 1000.00 729.1
373.24 5000.00 734.5
373.24 10000.00 740.8
373.24 15000.00 746.6
373.24 20000.00 751.9
373.24 25000.00 757.0
373.24 30000.00 761.6
373.24 35000.00 766.1
373.24 40000.00 770.4
373.24 45000.00 774.4
373.24 50000.00 778.1
373.24 55000.00 781.9
373.24 60000.00 785.4
373.24 65000.00 788.8
373.24 70000.00 792.1
373.24 80000.00 798.5
373.24 90000.00 804.3
373.24 100000.00 809.8
373.24 110000.00 815.1
373.24 120000.00 820.1
373.24 130000.00 824.9
373.24 140000.00 829.5
393.27 1000.00 704.8
393.27 5000.00 711.4
393.27 10000.00 718.8
393.27 15000.00 725.6
393.27 20000.00 731.7
393.27 25000.00 737.4
393.27 30000.00 742.7
393.27 35000.00 747.8
393.27 40000.00 752.5
393.27 45000.00 757.0
393.27 50000.00 761.2
393.27 55000.00 765.4
393.27 60000.00 769.2
393.27 65000.00 773.0
393.27 70000.00 776.6
393.27 80000.00 783.4
393.27 90000.00 789.8
393.27 100000.00 795.8
393.27 110000.00 801.5
393.27 120000.00 806.8
393.27 130000.00 811.9
393.27 140000.00 816.8
Reference
Fixed Measured
Pressure, kPa - Liquid Temperature, K - Liquid Mass density, kg/m3 - Liquid
100.00 293.15 806.7
1000.00 293.15 807.4
5000.00 293.15 810.4
10000.00 293.15 814.0
15000.00 293.15 817.4
20000.00 293.15 820.7
25000.00 293.15 823.9
30000.00 293.15 826.9
35000.00 293.15 829.8
40000.00 293.15 832.7
45000.00 293.15 835.4
50000.00 293.15 838.1
55000.00 293.15 840.6
60000.00 293.15 843.2
65000.00 293.15 845.6
70000.00 293.15 848.0
80000.00 293.15 852.6
90000.00 293.15 857.1
100000.00 293.15 861.2
110000.00 293.15 865.3
120000.00 293.15 869.2
130000.00 293.15 873.0
140000.00 293.15 876.6
100.00 298.15 802.6
1000.00 298.15 803.3
5000.00 298.15 806.4
10000.00 298.15 810.1
15000.00 298.15 813.7
20000.00 298.15 817.0
25000.00 298.15 820.2
30000.00 298.15 823.4
35000.00 298.15 826.4
40000.00 298.15 829.2
45000.00 298.15 832.0
50000.00 298.15 834.7
55000.00 298.15 837.4
60000.00 298.15 839.9
65000.00 298.15 842.4
70000.00 298.15 844.8
80000.00 298.15 849.5
90000.00 298.15 854.1
100000.00 298.15 858.3
110000.00 298.15 862.4
120000.00 298.15 866.3
130000.00 298.15 870.1
140000.00 298.15 873.9
100.00 313.15 789.6
1000.00 313.15 790.3
5000.00 313.15 793.7
10000.00 313.15 797.8
15000.00 313.15 801.6
20000.00 313.15 805.3
25000.00 313.15 808.6
30000.00 313.15 812.1
35000.00 313.15 815.3
40000.00 313.15 818.4
45000.00 313.15 821.3
50000.00 313.15 824.3
55000.00 313.15 827.1
60000.00 313.15 829.8
65000.00 313.15 832.5
70000.00 313.15 835.0
80000.00 313.15 839.9
90000.00 313.15 844.7
100000.00 313.15 849.1
110000.00 313.15 853.5
120000.00 313.15 857.6
130000.00 313.15 861.5
140000.00 313.15 865.4
100.00 333.15 770.8
1000.00 333.15 771.8
5000.00 333.15 775.7
10000.00 333.15 780.3
15000.00 333.15 784.7
20000.00 333.15 788.9
25000.00 333.15 792.7
30000.00 333.15 796.4
35000.00 333.15 800.0
40000.00 333.15 803.5
45000.00 333.15 806.6
50000.00 333.15 809.8
55000.00 333.15 812.8
60000.00 333.15 815.8
65000.00 333.15 818.7
70000.00 333.15 821.4
80000.00 333.15 826.8
90000.00 333.15 831.9
100000.00 333.15 836.7
110000.00 333.15 841.3
120000.00 333.15 845.6
130000.00 333.15 849.9
140000.00 333.15 853.9
100.00 353.19 750.3
1000.00 353.19 751.4
5000.00 353.19 756.0
10000.00 353.19 761.3
15000.00 353.19 766.4
20000.00 353.19 771.0
25000.00 353.19 775.4
30000.00 353.19 779.5
35000.00 353.19 783.5
40000.00 353.19 787.2
45000.00 353.19 790.8
50000.00 353.19 794.4
55000.00 353.19 797.7
60000.00 353.19 801.0
65000.00 353.19 804.1
70000.00 353.19 807.2
80000.00 353.19 812.9
90000.00 353.19 818.3
100000.00 353.19 823.5
110000.00 353.19 828.5
120000.00 353.19 833.1
130000.00 353.19 837.6
140000.00 353.19 842.0
1000.00 373.24 729.1
5000.00 373.24 734.5
10000.00 373.24 740.8
15000.00 373.24 746.6
20000.00 373.24 751.9
25000.00 373.24 757.0
30000.00 373.24 761.6
35000.00 373.24 766.1
40000.00 373.24 770.3
45000.00 373.24 774.4
50000.00 373.24 778.1
55000.00 373.24 781.8
60000.00 373.24 785.3
65000.00 373.24 788.8
70000.00 373.24 792.1
80000.00 373.24 798.4
90000.00 373.24 804.3
100000.00 373.24 809.8
110000.00 373.24 815.1
120000.00 373.24 820.1
130000.00 373.24 824.9
140000.00 373.24 829.5
1000.00 393.28 704.8
5000.00 393.28 711.3
10000.00 393.28 718.8
15000.00 393.28 725.6
20000.00 393.28 731.7
25000.00 393.28 737.4
30000.00 393.28 742.7
35000.00 393.28 747.8
40000.00 393.28 752.5
45000.00 393.28 757.0
50000.00 393.28 761.2
55000.00 393.28 765.4
60000.00 393.28 769.2
65000.00 393.28 772.9
70000.00 393.28 776.6
80000.00 393.28 783.4
90000.00 393.28 789.8
100000.00 393.28 795.8
110000.00 393.28 801.5
120000.00 393.28 806.8
130000.00 393.28 811.9
140000.00 393.28 816.8
Reference
Fixed Measured
Pressure, kPa - Liquid Temperature, K - Liquid Mass density, kg/m3 - Liquid
100.00 273.15 822.3
1000.00 273.15 822.7
2000.00 273.15 823.4
5000.00 273.15 825.4
10000.00 273.15 828.7
15000.00 273.15 831.8
20000.00 273.15 834.7
30000.00 273.15 840.4
40000.00 273.15 845.7
50000.00 273.15 850.7
60000.00 273.15 855.4
70000.00 273.15 859.9
80000.00 273.15 864.3
90000.00 273.15 868.4
100000.00 273.15 872.4
110000.00 273.15 876.3
120000.00 273.15 879.9
130000.00 273.15 883.5
140000.00 273.15 887.2
100.00 293.15 806.3
1000.00 293.15 807.0
2000.00 293.15 807.8
5000.00 293.15 810.0
10000.00 293.15 813.6
15000.00 293.15 817.0
20000.00 293.15 820.2
30000.00 293.15 826.5
40000.00 293.15 832.3
50000.00 293.15 837.7
60000.00 293.15 842.8
70000.00 293.15 847.7
80000.00 293.15 852.3
90000.00 293.15 856.7
100000.00 293.15 860.9
110000.00 293.15 865.0
120000.00 293.15 868.8
130000.00 293.15 872.7
140000.00 293.15 876.3
100.00 313.15 789.4
1000.00 313.15 790.1
2000.00 313.15 791.0
5000.00 313.15 793.5
10000.00 313.15 797.5
15000.00 313.15 801.4
20000.00 313.15 805.1
30000.00 313.15 811.9
40000.00 313.15 818.3
50000.00 313.15 824.1
60000.00 313.15 829.6
70000.00 313.15 835.0
80000.00 313.15 839.9
90000.00 313.15 844.6
100000.00 313.15 849.0
110000.00 313.15 853.3
120000.00 313.15 857.5
130000.00 313.15 861.5
140000.00 313.15 865.4
100.00 333.15 770.7
1000.00 333.15 771.6
2000.00 333.15 772.6
5000.00 333.15 775.5
10000.00 333.15 780.1
15000.00 333.15 784.4
20000.00 333.15 788.6
30000.00 333.15 796.2
40000.00 333.15 803.2
50000.00 333.15 809.6
60000.00 333.15 815.7
70000.00 333.15 821.4
80000.00 333.15 826.7
90000.00 333.15 831.8
100000.00 333.15 836.6
110000.00 333.15 841.2
120000.00 333.15 845.5
130000.00 333.15 849.8
140000.00 333.15 853.9
Reference
Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
298.15 81.50 802.5
Reference
Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
323.16 83.00 780.1
343.15 90.00 760.2
358.15 94.00 744.2
298.15 96.00 802.3
313.15 97.00 789.4
328.15 97.00 775.5
303.15 98.00 798.2
288.15 99.00 810.8
293.15 99.00 806.7
308.15 99.00 793.9
283.15 99.00 814.7
338.15 99.00 765.5
348.15 99.00 755.0
363.15 99.00 738.7
333.15 100.00 770.5
353.15 101.00 749.7
318.15 102.00 784.8
308.15 284.00 794.1
318.15 288.00 785.0
303.15 290.00 798.3
343.15 290.00 760.5
298.15 291.00 802.5
338.15 292.00 765.7
348.15 293.00 755.2
288.15 298.00 811.0
293.16 304.00 806.8
283.15 306.00 814.8
353.15 309.00 749.9
323.16 310.00 780.3
358.15 317.00 744.5
328.16 325.00 775.7
313.15 331.00 789.6
363.15 349.00 739.0
333.15 350.00 770.7
303.16 469.00 798.5
343.15 469.00 760.6
318.16 476.00 785.1
298.15 488.00 802.7
353.15 488.00 750.2
333.15 494.00 770.9
308.15 499.00 794.3
293.16 505.00 807.0
288.15 511.00 811.1
363.15 512.00 739.3
313.15 521.00 789.8
283.15 529.00 815.0
358.15 531.00 744.8
323.15 539.00 780.5
338.15 539.00 766.0
328.15 549.00 775.9
348.15 632.00 755.6
293.15 891.00 807.3
338.15 892.00 766.4
333.15 901.00 771.3
323.16 904.00 780.9
298.16 906.00 803.0
283.15 909.00 815.3
318.15 909.00 785.5
328.16 909.00 776.3
343.15 910.00 761.1
363.15 910.00 739.8
288.15 912.00 811.4
358.15 912.00 745.3
303.15 914.00 798.8
308.16 919.00 794.6
313.15 925.00 790.2
348.15 926.00 756.0
353.15 937.00 750.7
288.15 993.00 811.5
298.15 995.00 803.1
353.15 997.00 750.8
358.16 997.00 745.3
318.16 1004.00 785.6
338.15 1007.00 766.5
348.15 1007.00 756.0
333.15 1016.00 771.5
303.15 1019.00 798.9
328.16 1025.00 776.4
293.16 1026.00 807.4
323.15 1027.00 781.0
308.15 1030.00 794.8
283.15 1030.00 815.4
343.15 1032.00 761.3
363.16 1038.00 739.9
313.16 1053.00 790.3
313.15 1936.00 791.0
348.15 1961.00 757.1
318.16 1987.00 786.5
293.16 1994.00 808.2
343.15 1994.00 762.3
333.15 2000.00 772.4
358.15 2002.00 746.6
283.15 2005.00 816.1
303.15 2009.00 799.7
308.15 2012.00 795.6
363.16 2013.00 741.2
298.15 2020.00 803.9
323.16 2023.00 781.9
328.16 2032.00 777.5
353.15 2036.00 752.0
288.15 2048.00 812.3
338.16 2082.00 767.6
358.16 2956.00 747.8
343.16 2963.00 763.4
313.15 2964.00 791.9
323.16 2969.00 782.8
348.15 2971.00 758.2
353.16 2973.00 753.1
328.15 2980.00 778.3
283.15 2987.00 816.8
303.15 3007.00 800.5
293.16 3011.00 808.9
308.15 3016.00 796.4
288.15 3020.00 813.0
333.15 3021.00 773.4
318.16 3033.00 787.4
298.16 3037.00 804.7
363.15 3038.00 742.5
338.15 3160.00 768.7
358.16 4886.00 750.1
348.15 4887.00 760.3
338.15 4911.00 770.5
303.15 4968.00 802.1
283.15 4975.00 818.2
343.15 4978.00 765.5
293.16 4984.00 810.4
328.16 4986.00 780.3
313.16 5002.00 793.7
333.15 5004.00 775.4
323.15 5007.00 784.7
308.16 5009.00 798.1
318.16 5011.00 789.2
353.15 5052.00 755.5
298.16 5064.00 806.3
363.16 5065.00 745.0
288.15 5097.00 814.5
348.15 6901.00 762.5
338.16 6964.00 772.5
318.16 6978.00 790.9
358.15 6978.00 752.5
313.16 6986.00 795.3
328.15 6989.00 782.1
288.16 6990.00 815.8
283.15 6996.00 819.6
293.16 7001.00 811.9
308.16 7020.00 799.7
303.16 7034.00 803.7
353.15 7035.00 757.6
363.16 7039.00 747.4
343.15 7040.00 767.6
323.15 7056.00 786.5
298.16 7065.00 807.8
333.15 7066.00 777.4
353.15 8919.00 759.7
303.15 8967.00 805.2
293.16 8967.00 813.4
363.16 8975.00 749.7
313.16 8976.00 797.0
338.16 8976.00 774.5
348.15 8976.00 764.6
333.15 8994.00 779.1
358.15 8996.00 754.7
283.15 9019.00 821.0
298.15 9025.00 809.3
328.15 9026.00 784.0
308.16 9036.00 801.3
343.15 9056.00 769.6
323.15 9085.00 788.3
288.16 9100.00 817.3
318.15 9293.00 792.8
303.16 9943.00 806.0
363.16 10001.00 750.8
288.15 10002.00 818.0
318.16 10006.00 793.4
308.15 10011.00 802.0
293.15 10027.00 814.1
333.15 10031.00 780.0
283.15 10037.00 821.7
338.15 10039.00 775.5
348.15 10049.00 765.7
298.15 10078.00 810.0
313.15 10109.00 797.8
358.16 10124.00 755.9
343.15 10137.00 770.7
353.15 10172.00 761.0
328.15 10174.00 785.0
323.15 10245.00 789.3
303.16 11919.00 807.5
288.15 11924.00 819.3
358.16 11961.00 757.9
308.16 11963.00 803.6
333.15 11980.00 781.8
338.15 12002.00 777.3
293.15 12006.00 815.5
283.15 12013.00 823.0
298.16 12017.00 811.4
318.15 12039.00 795.1
313.15 12051.00 799.4
328.16 12064.00 786.6
353.16 12072.00 762.9
343.15 12089.00 772.5
323.15 12118.00 790.8
348.15 12159.00 767.9
363.15 12190.00 753.3
343.15 14318.00 774.6
363.16 14664.00 755.9
358.15 14843.00 760.9
283.15 14917.00 824.9
293.15 14925.00 817.5
353.15 14941.00 765.8
318.15 14977.00 797.4
313.16 14996.00 801.7
328.15 15005.00 789.1
308.16 15014.00 805.8
333.15 15020.00 784.5
323.15 15027.00 793.2
303.16 15070.00 809.8
288.15 15086.00 821.4
348.15 15134.00 770.8
338.15 15149.00 780.1
343.15 15186.00 775.4
298.16 15244.00 813.7
363.16 17691.00 759.0
293.16 17912.00 819.5
308.15 17937.00 808.0
298.15 17949.00 815.6
283.15 17956.00 826.9
328.15 17974.00 791.5
313.16 17980.00 803.9
303.15 17980.00 811.8
333.15 17985.00 786.9
288.15 17992.00 823.4
358.16 17993.00 764.1
343.15 17997.00 777.9
318.15 17998.00 799.8
348.15 18029.00 773.4
323.15 18033.00 795.6
338.15 18051.00 782.6
353.16 18090.00 768.8
298.15 19932.00 817.0
308.16 19942.00 809.4
343.15 19975.00 779.7
288.15 19982.00 824.6
338.15 19986.00 784.2
313.16 20012.00 805.4
318.15 20024.00 801.3
283.15 20028.00 828.2
348.15 20029.00 775.3
303.15 20032.00 813.3
293.16 20060.00 821.0
328.16 20081.00 793.3
358.15 20099.00 766.2
363.16 20116.00 761.4
323.15 20133.00 797.2
353.15 20147.00 770.7
333.16 20151.00 788.8
303.15 21980.00 814.6
288.15 21991.00 825.9
283.15 21997.00 829.4
338.15 21999.00 785.9
358.15 22025.00 767.9
293.15 22039.00 822.3
313.15 22039.00 806.9
318.16 22040.00 802.8
333.15 22042.00 790.2
343.15 22054.00 781.5
298.15 22061.00 818.4
323.16 22069.00 798.7
363.16 22089.00 763.4
348.15 22105.00 777.1
328.15 22112.00 794.8
308.16 22125.00 810.9
353.15 22188.00 772.6
318.15 24907.00 804.9
348.15 24943.00 779.5
293.15 24969.00 824.2
283.15 24984.00 831.2
313.15 24988.00 809.0
338.16 24990.00 788.3
298.15 24991.00 820.3
308.16 25007.00 813.0
328.16 25008.00 797.1
358.15 25009.00 770.7
323.15 25015.00 800.9
353.15 25053.00 775.1
333.15 25059.00 792.7
303.15 25089.00 816.7
363.15 25101.00 766.2
343.15 25145.00 784.1
288.15 25200.00 827.9
298.15 27926.00 822.2
348.15 27937.00 782.1
358.16 27942.00 773.3
338.16 27960.00 790.7
313.15 27962.00 811.0
343.15 27969.00 786.3
318.15 27973.00 807.1
303.15 27989.00 818.6
283.15 27996.00 833.0
293.15 28001.00 826.0
308.16 28001.00 815.0
363.16 28014.00 768.8
353.15 28045.00 777.7
333.15 28048.00 794.9
328.15 28057.00 799.3
323.15 28096.00 803.1
288.15 28149.00 829.7
283.15 29889.00 834.1
348.15 29922.00 783.7
333.15 29961.00 796.3
318.15 30001.00 808.5
293.15 30012.00 827.2
313.15 30012.00 812.4
303.15 30014.00 819.9
328.15 30020.00 800.7
323.16 30034.00 804.5
363.15 30034.00 770.6
308.16 30046.00 816.3
288.15 30056.00 830.8
338.16 30065.00 792.3
358.16 30089.00 775.1
298.15 30121.00 823.6
353.15 30122.00 779.4
343.15 30130.00 788.1
343.15 31848.00 789.4
338.16 31895.00 793.7
283.15 31914.00 835.3
353.15 31946.00 780.9
308.15 31948.00 817.5
293.15 31992.00 828.4
303.16 31992.00 821.1
288.15 32010.00 832.0
323.16 32030.00 805.9
313.15 32043.00 813.7
348.15 32051.00 785.4
298.15 32061.00 824.8
318.16 32063.00 809.9
358.16 32063.00 776.8
363.16 32089.00 772.4
328.15 32096.00 802.2
333.15 32126.00 798.0
333.15 32780.00 798.4
353.15 32790.00 781.6
353.15 32795.00 781.5
333.15 32804.00 798.4
318.15 32873.00 810.4
343.15 32904.00 790.1
288.15 32915.00 832.4
303.15 32951.00 821.7
308.15 32957.00 818.2
338.15 32975.00 794.4
288.15 32978.00 832.5
338.16 32982.00 794.5
363.15 33002.00 773.1
303.15 33007.00 821.7
343.15 33014.00 790.3
308.15 33017.00 818.2
318.15 33033.00 810.4
313.15 33039.00 814.4
298.15 33040.00 825.4
363.15 33042.00 773.2
283.15 33047.00 835.9
358.15 33055.00 777.5
283.15 33065.00 835.9
293.15 33079.00 829.1
313.15 33084.00 814.4
298.15 33088.00 825.4
348.15 33089.00 786.2
328.15 33090.00 802.9
358.15 33103.00 777.7
293.16 33109.00 829.0
323.15 33113.00 806.7
348.15 33156.00 786.2
323.16 33179.00 806.7
328.16 33187.00 802.9
288.15 33919.00 833.0
343.15 33950.00 790.9
338.16 33953.00 795.1
333.15 33981.00 799.2
318.16 33988.00 811.1
303.15 33998.00 822.3
283.15 34001.00 836.4
308.15 34003.00 818.8
298.16 34019.00 825.9
353.15 34025.00 782.5
293.15 34051.00 829.6
363.15 34072.00 774.0
323.16 34081.00 807.3
348.15 34089.00 786.8
313.16 34096.00 815.0
328.15 34106.00 803.6
358.15 34173.00 778.4
283.15 34979.00 836.9
318.16 34997.00 811.8
293.16 35005.00 830.2
343.15 35008.00 791.7
298.15 35034.00 826.5
353.15 35037.00 783.3
313.16 35045.00 815.6
288.16 35048.00 833.7
308.16 35061.00 819.4
303.16 35073.00 823.0
333.15 35081.00 800.0
363.16 35096.00 775.0
348.15 35121.00 787.6
338.15 35130.00 796.0
323.16 35135.00 808.0
328.16 35148.00 804.3
358.15 35154.00 779.2
313.15 37907.00 817.5
283.16 37912.00 838.6
338.16 37933.00 798.0
293.15 37933.00 831.9
363.16 37960.00 777.4
288.15 37967.00 835.3
348.15 37976.00 789.8
323.15 37980.00 809.9
308.15 38001.00 821.3
328.15 38003.00 806.3
358.15 38016.00 781.5
298.15 38020.00 828.3
318.16 38029.00 813.7
333.15 38040.00 802.1
303.15 38048.00 824.8
353.16 38061.00 785.7
343.15 38168.00 794.1
343.15 39957.00 795.4
353.15 39961.00 787.1
318.16 39963.00 815.0
333.15 39970.00 803.4
283.15 40002.00 839.7
303.15 40020.00 826.0
298.16 40026.00 829.5
348.15 40028.00 791.3
358.15 40036.00 783.1
363.15 40041.00 779.0
308.16 40051.00 822.5
323.15 40058.00 811.2
288.15 40071.00 836.5
338.15 40077.00 799.5
293.15 40088.00 833.1
313.16 40135.00 818.9
328.15 40189.00 807.7
308.16 41974.00 823.7
338.16 41987.00 800.8
343.15 42001.00 796.8
303.15 42004.00 827.1
288.15 42013.00 837.6
298.16 42019.00 830.7
323.15 42026.00 812.5
313.15 42039.00 820.0
353.15 42055.00 788.7
293.15 42062.00 834.2
358.15 42070.00 784.7
283.15 42074.00 840.9
333.16 42099.00 804.9
348.15 42107.00 792.9
318.16 42133.00 816.4
328.15 42227.00 809.1
363.15 42237.00 780.7
348.15 44933.00 794.9
338.15 44943.00 802.8
358.15 44944.00 786.8
363.15 44948.00 782.8
323.16 44962.00 814.4
343.15 44975.00 798.9
283.15 44993.00 842.4
298.16 44993.00 832.3
303.15 44999.00 828.9
313.16 45006.00 821.8
308.15 45022.00 825.5
353.15 45025.00 790.9
293.15 45052.00 835.9
288.15 45099.00 839.3
333.15 45112.00 806.9
328.16 45203.00 811.1
318.15 45210.00 818.3
303.15 45386.00 829.1
353.15 47906.00 793.0
358.15 47921.00 789.0
298.16 47933.00 834.0
333.15 47953.00 808.7
288.15 47977.00 840.8
343.15 47992.00 801.0
308.16 47997.00 827.2
323.16 48021.00 816.3
338.15 48022.00 804.9
283.15 48024.00 844.0
363.15 48033.00 785.1
348.15 48043.00 797.1
318.15 48072.00 820.1
313.16 48081.00 823.7
293.15 48098.00 837.6
328.16 48119.00 812.8
303.15 48182.00 830.7
298.15 49981.00 835.1
343.15 49990.00 802.3
318.15 49996.00 821.2
353.16 49998.00 794.4
293.15 50000.00 838.6
313.15 50005.00 824.8
308.15 50010.00 828.4
363.15 50015.00 786.6
328.16 50027.00 814.0
338.16 50029.00 806.2
323.15 50034.00 817.5
358.15 50038.00 790.5
283.15 50047.00 845.1
333.15 50048.00 810.1
288.16 50052.00 842.0
303.15 50063.00 831.8
348.15 50077.00 798.4
303.15 51975.00 832.8
288.15 51983.00 842.9
318.16 51984.00 822.4
353.15 51988.00 795.8
293.15 51999.00 839.7
343.15 52005.00 803.6
308.15 52016.00 829.5
313.16 52025.00 826.0
283.15 52032.00 846.1
298.16 52047.00 836.3
338.15 52052.00 807.5
333.15 52052.00 811.3
323.15 52055.00 818.7
358.15 52069.00 792.0
348.15 52078.00 799.8
363.15 52088.00 788.1
328.16 52217.00 815.4
348.15 54947.00 801.7
288.16 54961.00 844.5
298.16 54969.00 837.8
353.16 54972.00 797.7
318.16 54987.00 824.1
308.15 54994.00 831.2
333.15 55007.00 813.2
323.16 55018.00 820.5
313.16 55030.00 827.7
363.15 55038.00 790.2
283.15 55041.00 847.6
343.15 55047.00 805.7
303.16 55053.00 834.5
293.15 55060.00 841.3
358.15 55065.00 794.1
338.15 55069.00 809.5
328.16 55140.00 817.1
283.15 57909.00 849.1
318.15 57926.00 825.8
343.15 57941.00 807.5
323.15 57941.00 822.2
303.16 57971.00 836.1
288.15 57976.00 846.0
298.15 57978.00 839.4
363.15 57996.00 792.2
333.16 58002.00 815.0
353.15 58003.00 799.9
348.15 58004.00 803.6
308.15 58005.00 832.8
328.16 58016.00 818.7
358.15 58024.00 796.1
313.15 58031.00 829.3
338.15 58033.00 811.3
293.15 58191.00 842.9
303.16 59945.00 837.1
288.16 59961.00 847.0
328.16 59968.00 819.8
343.15 59985.00 808.8
313.16 60001.00 830.4
318.16 60004.00 827.0
333.16 60019.00 816.2
308.15 60029.00 833.9
283.15 60034.00 850.1
353.16 60035.00 801.2
298.15 60039.00 840.5
323.16 60048.00 823.4
358.15 60060.00 797.4
293.16 60071.00 843.8
363.15 60085.00 793.7
348.15 60105.00 805.1
338.15 60108.00 812.6
343.15 61963.00 810.0
328.16 61968.00 820.9
308.16 61986.00 835.0
318.16 62005.00 828.1
303.16 62023.00 838.2
333.15 62024.00 817.4
283.15 62037.00 851.1
288.15 62043.00 848.0
338.15 62047.00 813.7
298.15 62048.00 841.5
293.15 62049.00 844.8
313.16 62068.00 831.6
363.15 62081.00 795.0
323.16 62109.00 824.6
353.15 62118.00 802.6
348.15 62134.00 806.4
358.15 62217.00 798.9
303.16 64910.00 839.7
348.15 64952.00 808.1
293.15 64958.00 846.3
333.15 64970.00 819.1
343.15 64974.00 811.9
308.16 64977.00 836.6
288.15 64998.00 849.5
338.15 65005.00 815.5
318.16 65012.00 829.7
328.16 65013.00 822.7
353.15 65015.00 804.4
363.15 65016.00 796.9
298.16 65037.00 843.1
323.15 65042.00 826.2
358.15 65051.00 800.7
313.16 65053.00 833.2
283.15 65102.00 852.6
363.15 66010.00 797.6
298.15 66054.00 843.6
313.16 66058.00 833.7
358.15 66079.00 801.3
283.15 66079.00 853.0
318.16 66081.00 830.3
348.15 66089.00 808.8
303.16 66100.00 840.3
333.15 66117.00 819.8
338.15 66128.00 816.2
308.16 66129.00 837.2
343.16 66132.00 812.5
328.16 66143.00 823.3
288.15 66143.00 850.0
293.15 66185.00 846.9
323.16 66222.00 826.9
353.15 66227.00 805.2
Reference
Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
298.15 100.00 802.5
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
253.15 100.00 1374.557
253.15 5155.00 1400.286
253.15 10194.00 1424.811
253.15 15178.00 1448.123
253.15 20139.00 1470.454
253.15 25051.00 1491.936
253.15 30449.00 1514.428
273.15 100.00 1301.188
273.15 5150.00 1329.213
273.15 10187.00 1355.764
273.15 15226.00 1381.12
273.15 20096.00 1404.617
273.15 25052.00 1427.686
273.15 30040.00 1450.042
293.15 102.00 1229.105
293.15 5048.00 1258.924
293.15 10078.00 1287.65
293.15 15045.00 1314.609
293.15 20093.00 1340.859
293.15 25164.00 1366.019
293.15 29995.00 1389.034
313.15 100.00 1156.286
313.15 5081.00 1189.239
313.15 10051.00 1219.979
313.15 15034.00 1249.234
313.15 20050.00 1277.226
313.15 25148.00 1304.343
313.15 30041.00 1329.278
333.15 101.00 1081.368
333.15 5111.00 1117.787
333.15 10069.00 1151.366
333.15 15039.00 1183.013
333.15 20109.00 1213.479
333.15 25122.00 1242.123
333.15 30086.00 1269.15
353.15 119.00 1003.728
353.15 5050.00 1043.556
353.15 10149.00 1081.484
353.15 15213.00 1116.548
353.15 20040.00 1147.916
353.15 25218.00 1179.687
353.15 30032.00 1207.692
Reference

Correlations

Property Value Unit Temperature (K) Source
Cp,gas [76.82; 285.33] J/mol×K [150.00; 1500.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is Cp,gas in J/mol×K, T in K
Coefficient A7.03190e+01
Coefficient B-5.64510e+02
Coefficient C5.60924e+00
Coefficient D1.86610e-04
Coefficient E-6.31660e-08
Temperature range, min.150.00
Temperature range, max.1500.00
Cp,gas 76.82 J/mol×K 150.00 Calculated Property
Cp,gas 114.04 J/mol×K 300.00 Calculated Property
Cp,gas 153.91 J/mol×K 450.00 Calculated Property
Cp,gas 186.79 J/mol×K 600.00 Calculated Property
Cp,gas 213.05 J/mol×K 750.00 Calculated Property
Cp,gas 234.14 J/mol×K 900.00 Calculated Property
Cp,gas 251.21 J/mol×K 1050.00 Calculated Property
Cp,gas 265.08 J/mol×K 1200.00 Calculated Property
Cp,gas 276.32 J/mol×K 1350.00 Calculated Property
Cp,gas 285.33 J/mol×K 1500.00 Calculated Property
Property Value Unit Temperature (K) Source
Cp,liquid [129.81; 279.62] J/mol×K [158.45; 372.70] 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 A6.85130e+01
Coefficient B6.31420e+02
Coefficient C-4.16526e+00
Coefficient D3.16400e-02
Coefficient E-2.85720e-05
Temperature range, min.158.45
Temperature range, max.372.70
Cp,liquid 129.81 J/mol×K 158.45 Calculated Property
Cp,liquid 129.87 J/mol×K 182.26 Calculated Property
Cp,liquid 135.57 J/mol×K 206.06 Calculated Property
Cp,liquid 145.60 J/mol×K 229.87 Calculated Property
Cp,liquid 159.57 J/mol×K 253.67 Calculated Property
Cp,liquid 177.35 J/mol×K 277.48 Calculated Property
Cp,liquid 198.78 J/mol×K 301.28 Calculated Property
Cp,liquid 223.49 J/mol×K 325.09 Calculated Property
Cp,liquid 250.79 J/mol×K 348.89 Calculated Property
Cp,liquid 279.62 J/mol×K 372.70 Calculated Property
Property Value Unit Temperature (K) Source
η [0.0047154; 0.0002835] Pa×s [288.15; 400.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = exp(A + B/T + C·ln(T) + D·T^E)
Y is η in Pa×s, T in K
Coefficient A1.93290e+01
Coefficient B3.02690e+03
Coefficient C-6.65320e+00
Coefficient D2.99860e-05
Coefficient E2.00000e+00
Temperature range, min.288.15
Temperature range, max.400.00
η 0.0047154 Pa×s 288.15 Calculated Property
η 0.0028719 Pa×s 300.58 Calculated Property
η 0.0018482 Pa×s 313.01 Calculated Property
η 0.0012508 Pa×s 325.43 Calculated Property
η 0.0008865 Pa×s 337.86 Calculated Property
η 0.0006556 Pa×s 350.29 Calculated Property
η 0.0005043 Pa×s 362.72 Calculated Property
η 0.0004025 Pa×s 375.14 Calculated Property
η 0.0003324 Pa×s 387.57 Calculated Property
η 0.0002835 Pa×s 400.00 Calculated Property
Property Value Unit Temperature (K) Source
ΔvapH [63.11; 14.03] kJ/mol [158.45; 516.32] 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 A9.12377e+01
Coefficient B1.77973e+00
Coefficient C-3.38985e+00
Coefficient D3.54649e+00
Coefficient E-1.38526e+00
Critical temperature, Tc (K)5.36050e+02
Temperature range, min.158.45
Temperature range, max.516.32
ΔvapH 63.11 kJ/mol 158.45 Calculated Property
ΔvapH 59.09 kJ/mol 198.21 Calculated Property
ΔvapH 55.32 kJ/mol 237.98 Calculated Property
ΔvapH 51.52 kJ/mol 277.74 Calculated Property
ΔvapH 47.47 kJ/mol 317.50 Calculated Property
ΔvapH 42.97 kJ/mol 357.27 Calculated Property
ΔvapH 37.86 kJ/mol 397.03 Calculated Property
ΔvapH 31.91 kJ/mol 436.79 Calculated Property
ΔvapH 24.63 kJ/mol 476.56 Calculated Property
ΔvapH 14.03 kJ/mol 516.32 Calculated Property
Property Value Unit Temperature (K) Source
Pvap [1.33; 202.66] kPa [289.61; 391.83] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.52865e+01
Coefficient B-3.04428e+03
Coefficient C-8.66400e+01
Temperature range, min.289.61
Temperature range, max.391.83
Pvap 1.33 kPa 289.61 Calculated Property
Pvap 2.95 kPa 300.97 Calculated Property
Pvap 6.03 kPa 312.33 Calculated Property
Pvap 11.52 kPa 323.68 Calculated Property
Pvap 20.72 kPa 335.04 Calculated Property
Pvap 35.41 kPa 346.40 Calculated Property
Pvap 57.85 kPa 357.76 Calculated Property
Pvap 90.86 kPa 369.11 Calculated Property
Pvap 137.82 kPa 380.47 Calculated Property
Pvap 202.66 kPa 391.83 Calculated Property
Pvap [1.51e-09; 4160.36] kPa [158.45; 536.05] 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 A1.38642e+02
Coefficient B-1.08110e+04
Coefficient C-1.79570e+01
Coefficient D9.41320e-06
Coefficient E2.00000e+00
CommentRange stopped at Tc; ChemSep gives it to 536.2 K.
Temperature range, min.158.45
Temperature range, max.536.05
Pvap 1.51e-09 kPa 158.45 Calculated Property
Pvap 4.09e-05 kPa 200.41 Calculated Property
Pvap 0.02 kPa 242.36 Calculated Property
Pvap 0.92 kPa 284.32 Calculated Property
Pvap 13.19 kPa 326.27 Calculated Property
Pvap 86.18 kPa 368.23 Calculated Property
Pvap 340.14 kPa 410.18 Calculated Property
Pvap 959.95 kPa 452.14 Calculated Property
Pvap 2159.19 kPa 494.09 Calculated Property
Pvap 4160.36 kPa 536.05 Calculated Property
Pvap [3.09e-09; 4349.86] kPa [158.45; 536.01] 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 A1.03633e+02
Coefficient B-9.51804e+03
Coefficient C-1.24851e+01
Coefficient D3.34249e-06
Coefficient E0.00000e+00
Temperature range, min.158.45
Temperature range, max.536.01
Pvap 3.09e-09 kPa 158.45 Calculated Property
Pvap 5.00e-05 kPa 200.40 Calculated Property
Pvap 0.02 kPa 242.35 Calculated Property
Pvap 0.89 kPa 284.30 Calculated Property
Pvap 12.88 kPa 326.25 Calculated Property
Pvap 87.05 kPa 368.21 Calculated Property
Pvap 355.10 kPa 410.16 Calculated Property
Pvap 1023.28 kPa 452.11 Calculated Property
Pvap 2305.81 kPa 494.06 Calculated Property
Pvap 4349.86 kPa 536.01 Calculated Property
Pvap [472.26; 4161.87] kPa [422.11; 535.90] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.42720e+01
Coefficient B-2.51961e+03
Coefficient C-1.11603e+02
ReferenceAmbrose and Townsend, 1963, 2
CommentCoefficents calculated by NIST from author's data.
Temperature range, min.422.11
Temperature range, max.535.90
Pvap 472.26 kPa 422.11 Calculated Property
Pvap 648.73 kPa 434.75 Calculated Property
Pvap 870.08 kPa 447.40 Calculated Property
Pvap 1142.37 kPa 460.04 Calculated Property
Pvap 1471.53 kPa 472.68 Calculated Property
Pvap 1863.35 kPa 485.33 Calculated Property
Pvap 2323.31 kPa 497.97 Calculated Property
Pvap 2856.60 kPa 510.61 Calculated Property
Pvap 3468.00 kPa 523.26 Calculated Property
Pvap 4161.87 kPa 535.90 Calculated Property
Pvap [33.02; 133.51] kPa [345.54; 380.30] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.45741e+01
Coefficient B-2.66794e+03
Coefficient C-1.04683e+02
ReferenceBiddiscombe, Collerson, et al., 1963, 2
CommentCoefficents calculated by NIST from author's data.
Temperature range, min.345.54
Temperature range, max.380.30
Pvap 33.02 kPa 345.54 Calculated Property
Pvap 39.33 kPa 349.40 Calculated Property
Pvap 46.59 kPa 353.26 Calculated Property
Pvap 54.90 kPa 357.13 Calculated Property
Pvap 64.38 kPa 360.99 Calculated Property
Pvap 75.14 kPa 364.85 Calculated Property
Pvap 87.30 kPa 368.71 Calculated Property
Pvap 100.99 kPa 372.58 Calculated Property
Pvap 116.35 kPa 376.44 Calculated Property
Pvap 133.51 kPa 380.30 Calculated Property
Pvap [472.26; 4161.87] kPa [422.11; 535.90] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.42720e+01
Coefficient B-2.51961e+03
Coefficient C-1.11603e+02
ReferenceAmbrose and Townsend, 1963
CommentCoefficents calculated by NIST from author's data.
Temperature range, min.422.11
Temperature range, max.535.90
Pvap 472.26 kPa 422.11 Calculated Property
Pvap 648.73 kPa 434.75 Calculated Property
Pvap 870.08 kPa 447.40 Calculated Property
Pvap 1142.37 kPa 460.04 Calculated Property
Pvap 1471.53 kPa 472.68 Calculated Property
Pvap 1863.35 kPa 485.33 Calculated Property
Pvap 2323.31 kPa 497.97 Calculated Property
Pvap 2856.60 kPa 510.61 Calculated Property
Pvap 3468.00 kPa 523.26 Calculated Property
Pvap 4161.87 kPa 535.90 Calculated Property
Pvap [33.02; 133.51] kPa [345.54; 380.30] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.45741e+01
Coefficient B-2.66794e+03
Coefficient C-1.04683e+02
ReferenceBiddiscombe, Collerson, et al., 1963
CommentCoefficents calculated by NIST from author's data.
Temperature range, min.345.54
Temperature range, max.380.30
Pvap 33.02 kPa 345.54 Calculated Property
Pvap 39.33 kPa 349.40 Calculated Property
Pvap 46.59 kPa 353.26 Calculated Property
Pvap 54.90 kPa 357.13 Calculated Property
Pvap 64.38 kPa 360.99 Calculated Property
Pvap 75.14 kPa 364.85 Calculated Property
Pvap 87.30 kPa 368.71 Calculated Property
Pvap 100.99 kPa 372.58 Calculated Property
Pvap 116.35 kPa 376.44 Calculated Property
Pvap 133.51 kPa 380.30 Calculated Property
Property Value Unit Temperature (K) Source
ρl [925.32; 468.72] kg/m3 [158.45; 516.32] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A / B^(1 + (1 − T/C)^D)
Y is ρl in kg/m3, T in K
Coefficient A4.82094e+01
Coefficient B2.15580e-01
Coefficient C5.36050e+02
Coefficient D2.20840e-01
Temperature range, min.158.45
Temperature range, max.516.32
ρl 925.32 kg/m3 158.45 Calculated Property
ρl 893.97 kg/m3 198.21 Calculated Property
ρl 860.81 kg/m3 237.98 Calculated Property
ρl 825.44 kg/m3 277.74 Calculated Property
ρl 787.29 kg/m3 317.50 Calculated Property
ρl 745.45 kg/m3 357.27 Calculated Property
ρl 698.49 kg/m3 397.03 Calculated Property
ρl 643.72 kg/m3 436.79 Calculated Property
ρl 574.94 kg/m3 476.56 Calculated Property
ρl 468.72 kg/m3 516.32 Calculated Property
Property Value Unit Temperature (K) Source
γ [0.03; 0.02] N/m [273.15; 372.70] 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-1.34680e-02
Coefficient B-1.24810e+02
Coefficient C-1.73900e+00
Coefficient D-4.06530e-03
Coefficient E6.63830e-07
Temperature range, min.273.15
Temperature range, max.372.70
γ 0.03 N/m 273.15 Calculated Property
γ 0.02 N/m 284.21 Calculated Property
γ 0.02 N/m 295.27 Calculated Property
γ 0.02 N/m 306.33 Calculated Property
γ 0.02 N/m 317.39 Calculated Property
γ 0.02 N/m 328.46 Calculated Property
γ 0.02 N/m 339.52 Calculated Property
γ 0.02 N/m 350.58 Calculated Property
γ 0.02 N/m 361.64 Calculated Property
γ 0.02 N/m 372.70 Calculated Property
Property Value Unit Temperature (K) Source
λgas [0.01; 0.12] W/m×K [255.93; 992.70] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A·T^B / (1 + C/T + D/T²)
Y is λgas in W/m×K, T in K
Coefficient A1.16610e-06
Coefficient B1.70560e+00
Coefficient C3.40330e+02
Coefficient D-6.05530e+04
Temperature range, min.255.93
Temperature range, max.992.70
λgas 0.01 W/m×K 255.93 Calculated Property
λgas 0.02 W/m×K 337.79 Calculated Property
λgas 0.02 W/m×K 419.65 Calculated Property
λgas 0.03 W/m×K 501.52 Calculated Property
λgas 0.04 W/m×K 583.38 Calculated Property
λgas 0.06 W/m×K 665.25 Calculated Property
λgas 0.07 W/m×K 747.11 Calculated Property
λgas 0.08 W/m×K 828.97 Calculated Property
λgas 0.10 W/m×K 910.84 Calculated Property
λgas 0.12 W/m×K 992.70 Calculated Property
Property Value Unit Temperature (K) Source
λliquid [0.16; 0.11] W/m×K [200.00; 398.15] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is λliquid in W/m×K, T in K
Coefficient A3.17110e-02
Coefficient B-1.58340e+02
Coefficient C-2.44910e-01
Coefficient D-5.74750e-03
Coefficient E2.59100e-06
Temperature range, min.200.00
Temperature range, max.398.15
λliquid 0.16 W/m×K 200.00 Calculated Property
λliquid 0.15 W/m×K 222.02 Calculated Property
λliquid 0.15 W/m×K 244.03 Calculated Property
λliquid 0.14 W/m×K 266.05 Calculated Property
λliquid 0.14 W/m×K 288.07 Calculated Property
λliquid 0.13 W/m×K 310.08 Calculated Property
λliquid 0.13 W/m×K 332.10 Calculated Property
λliquid 0.12 W/m×K 354.12 Calculated Property
λliquid 0.12 W/m×K 376.13 Calculated Property
λliquid 0.11 W/m×K 398.15 Calculated Property

Similar Compounds

2-Butanol, (R)-. (S)-butan-2-ol. 3-Pentanol. (R)-(-)-2-Pentanol. 2-Pentanol. (S)-(+)-2-Pentanol. DL-2,3-Butanediol. 2,3-Butanediol. 2,3-Butanediol, [S-(R*,R*)]-. meso-2,3-butanediol. 2,3-Butanediol, [R-(R*,R*)]-. 1,3-Butanediol, (R)-. 1,3-Butanediol. 1,3-Butanediol, (S)-. Cyclobutanol.

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Mixtures

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Sources

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