Chemical Properties of Acetone (CAS 67-64-1)

Acetone

InChI
InChI=1S/C3H6O/c1-3(2)4/h1-2H3
InChI Key
CSCPPACGZOOCGX-UHFFFAOYSA-N
Formula
C3H6O
SMILES
CC(C)=O
Molecular Weight1
58.08
CAS
67-64-1
Other Names
  • (CH3)2CO
  • 2-propanone
  • Chevron acetone
  • Dimethylformaldehyde
  • Dimethylketal
  • Ketone propane
  • Ketone, dimethyl-
  • Methyl ketone
  • NSC 135802
  • Rcra waste number U002
  • Sasetone
  • UN 1090
  • dimethyl ketone
  • propan-2-one
  • propanone
  • pyroacetic ether
  • «beta»-Ketopropane
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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 [0.3040; 0.3090]   Show Hide
ω 0.3090 PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω 0.3070 ChemSep v8.3 pure component data Compiled value
ω 0.3040 KDB
PAff [811.50; 815.20] kJ/mol Show Hide
PAff 812.00 kJ/mol NIST
PAff 815.20 kJ/mol NIST
PAff 814.30 kJ/mol NIST
PAff 812.60 ± 0.20 kJ/mol NIST
PAff 811.50 ± 3.40 kJ/mol NIST
PAff 811.50 ± 3.40 kJ/mol NIST
Tig [738.15; 738.15] K Show Hide
Tig 738.15 K KDB
Tig 738.15 K NCMS SOLV-DB
BasG [782.00; 784.70] kJ/mol Show Hide
BasG 782.10 kJ/mol NIST
BasG Outlier 784.70 kJ/mol NIST
BasG 782.20 kJ/mol NIST
BasG 782.00 ± 0.20 kJ/mol NIST
BasG 782.10 ± 1.50 kJ/mol NIST
BasG 782.10 ± 1.50 kJ/mol NIST
ΔcH°gas -1821.40 ± 0.84 kJ/mol NIST
ΔcH°liquid [-1804.20; -1772.00] kJ/mol Show Hide
ΔcH°liquid -1772.00 kJ/mol NIST
ΔcH°liquid -1804.20 kJ/mol NIST
μ [2.88; 2.90] debye Show Hide
μ 2.88 debye ChemSep v8.3 pure component data Compiled value
μ 2.90 debye KDB
η [0.0003000; 0.0003121] Pa×s Show Hide
η 0.0003121 Pa×s Densities and Viscosities of Binary Liquid Mixtures of Trichloroethylene and Tetrachloroethylene with Some Polar and Nonpolar Solvents
η 0.0003000 Pa×s Densities and Viscosities of 1-Butyl-3-methylimidazolium Tetrafluoroborate + Molecular Solvent Binary Mixtures
EA 0.00 eV NIST
εr 20.56 NCMS SOLV-DB
LFL 2.60 % in Air KDB
UFL 12.80 % in Air KDB
Tflash,cc [256.15; 257.59] K Show Hide
Tflash,cc 257.59 K KDB
Tflash,cc 256.15 K NCMS SOLV-DB
Tflash,oc 255.37 K KDB
ΔfG° [-153.20; -151.30] kJ/mol Show Hide
ΔfG° -151.30 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfG° -153.20 kJ/mol KDB
Rg 2.7400 KDB
ΔfH°gas [-218.50; -215.70] kJ/mol Show Hide
ΔfH°gas -216.07 ± 0.37 kJ/mol Active Thermochemical Tables 1.112, gas-phase enthalpies of formation Compiled value
ΔfH°gas -215.70 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfH°gas -217.70 kJ/mol KDB
ΔfH°gas -218.50 ± 0.59 kJ/mol NIST
ΔfH°gas -217.10 ± 0.50 kJ/mol NIST
ΔfH°gas -217.50 ± 0.67 kJ/mol NIST
ΔfH°gas -216.40 kJ/mol NIST
ΔfH°liquid -249.40 ± 0.63 kJ/mol NIST
ΔfusH° 5.12 kJ/mol Joback Calculated Property
ΔvapH° [29.70; 31.30] kJ/mol Show Hide
ΔvapH° 31.30 kJ/mol NCMS SOLV-DB
ΔvapH° 31.27 kJ/mol NIST
ΔvapH° 31.30 kJ/mol NIST
ΔvapH° 29.70 ± 0.00 kJ/mol NIST
IE [9.50; 9.80] eV Show Hide
IE 9.70 ± 0.01 eV NIST
IE 9.70 eV NIST
IE 9.69 ± 0.01 eV NIST
IE 9.68 eV NIST
IE 9.71 ± 0.01 eV NIST
IE 9.71 ± 0.03 eV NIST
IE 9.71 ± 0.01 eV NIST
IE 9.71 eV NIST
IE 9.71 eV NIST
IE 9.70 ± 0.00 eV NIST
IE 9.71 eV NIST
IE 9.71 ± 0.01 eV NIST
IE 9.75 ± 0.03 eV NIST
IE 9.72 eV NIST
IE 9.74 eV NIST
IE 9.71 ± 0.01 eV NIST
IE 9.74 ± 0.03 eV NIST
IE 9.68 eV NIST
IE 9.71 ± 0.01 eV NIST
IE 9.70 ± 0.10 eV NIST
IE 9.68 ± 0.02 eV NIST
IE 9.67 eV NIST
IE 9.71 ± 0.03 eV NIST
IE 9.71 ± 0.03 eV NIST
IE 9.69 ± 0.01 eV NIST
IE 9.71 eV NIST
IE Outlier 9.80 eV NIST
IE 9.72 eV NIST
IE 9.68 eV NIST
IE 9.71 ± 0.02 eV NIST
IE Outlier 9.50 eV NIST
IE 9.70 eV NIST
IE 9.71 eV NIST
IE 9.71 eV NIST
IE 9.72 eV NIST
log10WS 0.57 Relay (1.0) Calculated Property
logPoct/wat -0.240 NCMS SOLV-DB
McVol 54.700 ml/mol McGowan Calculated Property
NFPA Fire [%!d(float64=3); %!d(float64=3)]   Show Hide
NFPA Fire 3 KDB
NFPA Fire 3 NCMS SOLV-DB
NFPA Health [%!d(float64=1); %!d(float64=1)]   Show Hide
NFPA Health 1 KDB
NFPA Health 1 NCMS SOLV-DB
NFPA Safety 0 NCMS SOLV-DB
Pc [4700.00; 5290.00] kPa Show Hide
Pc 4700.00 kPa IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Pc 4701.48 kPa PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc 4700.00 kPa ChemSep v8.3 pure component data Compiled value
Pc 4700.00 kPa KDB
Pc 4700.00 ± 10.00 kPa NIST
Pc 4700.00 ± 6.00 kPa NIST
Pc 4758.22 ± 10.13 kPa NIST
Pc 5062.20 ± 50.66 kPa NIST
Pc 4700.00 ± 101.32 kPa NIST
Pc 4790.00 ± 34.50 kPa NIST
Pc 4720.00 ± 101.32 kPa NIST
Pc 4740.00 ± 405.30 kPa NIST
Pc Outlier 5290.00 ± 405.30 kPa NIST
pKa 24.20 NCMS SOLV-DB
Ptriple 2.79e-03 kPa ChemSep v8.3 pure component data Compiled value
ρc [234.06; 278.20] kg/m3 Show Hide
ρc 268.91 ± 2.90 kg/m3 NIST
ρc 234.06 ± 1.51 kg/m3 NIST
ρc 278.20 ± 9.87 kg/m3 NIST
ρc 272.97 ± 1.16 kg/m3 NIST
ρc 252.06 ± 1.74 kg/m3 NIST
Inp [437.00; 512.00]   Show Hide
Inp 470.23 NIST
Inp 470.90 NIST
Inp 470.70 NIST
Inp 470.10 NIST
Inp 469.67 NIST
Inp 469.50 NIST
Inp 469.28 NIST
Inp 469.41 NIST
Inp 470.00 NIST
Inp 470.00 NIST
Inp 469.00 NIST
Inp 469.00 NIST
Inp 481.00 NIST
Inp 484.00 NIST
Inp 477.00 NIST
Inp 478.00 NIST
Inp 488.70 NIST
Inp 488.20 NIST
Inp 485.00 NIST
Inp 497.00 NIST
Inp 475.00 NIST
Inp Outlier 437.00 NIST
Inp Outlier 437.00 NIST
Inp 450.00 NIST
Inp 443.50 NIST
Inp 465.00 NIST
Inp 441.00 NIST
Inp 444.00 NIST
Inp Outlier 439.00 NIST
Inp 459.00 NIST
Inp 443.00 NIST
Inp 472.00 NIST
Inp 450.00 NIST
Inp 475.00 NIST
Inp 450.00 NIST
Inp 447.00 NIST
Inp Outlier 439.00 NIST
Inp 503.00 NIST
Inp 477.55 NIST
Inp Outlier 510.00 NIST
Inp 470.00 NIST
Inp 503.00 NIST
Inp 500.00 NIST
Inp 475.30 NIST
Inp 481.00 NIST
Inp 481.00 NIST
Inp 500.00 NIST
Inp 488.60 NIST
Inp 471.00 NIST
Inp 474.00 NIST
Inp 468.00 NIST
Inp 466.00 NIST
Inp 471.00 NIST
Inp 480.00 NIST
Inp 472.00 NIST
Inp 473.00 NIST
Inp 472.00 NIST
Inp 470.00 NIST
Inp 466.00 NIST
Inp 468.00 NIST
Inp 466.00 NIST
Inp 479.00 NIST
Inp 500.00 NIST
Inp 496.00 NIST
Inp 496.00 NIST
Inp 472.00 NIST
Inp 502.00 NIST
Inp 502.00 NIST
Inp 487.00 NIST
Inp 476.60 NIST
Inp 503.00 NIST
Inp 500.00 NIST
Inp 487.00 NIST
Inp 474.00 NIST
Inp 474.00 NIST
Inp 500.00 NIST
Inp 509.00 NIST
Inp Outlier 512.00 NIST
Inp 459.00 NIST
Inp 471.00 NIST
Inp 450.00 NIST
Inp 476.00 NIST
Inp 501.00 NIST
Inp 470.00 NIST
Inp 470.00 NIST
Inp 450.00 NIST
Inp 497.00 NIST
Inp 472.00 NIST
Inp 500.00 NIST
Inp 460.00 NIST
Inp 473.00 NIST
Inp 473.00 NIST
Inp 473.00 NIST
Inp 465.00 NIST
Inp 460.00 NIST
Inp 469.00 NIST
Inp 491.00 NIST
Inp 474.00 NIST
Inp 484.00 NIST
Inp 468.00 NIST
Inp 469.00 NIST
Inp 478.00 NIST
Inp 503.00 NIST
Inp 500.00 NIST
Inp 470.23 NIST
Inp 469.50 NIST
Inp 469.00 NIST
Inp 478.00 NIST
Inp 475.00 NIST
Inp 465.00 NIST
Inp 443.00 NIST
Inp 447.00 NIST
Inp 479.00 NIST
Inp 502.00 NIST
Inp 477.55 NIST
Inp 468.00 NIST
Inp 471.00 NIST
Inp 470.00 NIST
Ip [775.00; 854.00]   Show Hide
Ip 843.50 NIST
Ip 835.00 NIST
Ip 837.50 NIST
Ip 840.80 NIST
Ip 832.00 NIST
Ip Outlier 847.00 NIST
Ip Outlier 785.00 NIST
Ip 842.00 NIST
Ip 824.00 NIST
Ip 821.00 NIST
Ip 813.00 NIST
Ip 814.00 NIST
Ip 814.00 NIST
Ip 814.00 NIST
Ip 820.00 NIST
Ip 818.00 NIST
Ip 794.00 NIST
Ip 809.00 NIST
Ip 813.00 NIST
Ip 834.00 NIST
Ip 842.00 NIST
Ip 814.00 NIST
Ip 821.30 NIST
Ip 814.00 NIST
Ip 802.00 NIST
Ip 813.00 NIST
Ip 818.00 NIST
Ip 811.00 NIST
Ip 816.00 NIST
Ip 822.00 NIST
Ip 813.00 NIST
Ip 814.00 NIST
Ip 819.00 NIST
Ip 813.00 NIST
Ip 812.00 NIST
Ip 830.00 NIST
Ip 808.00 NIST
Ip 808.00 NIST
Ip 834.00 NIST
Ip 832.00 NIST
Ip 841.00 NIST
Ip 821.00 NIST
Ip 812.00 NIST
Ip 811.00 NIST
Ip 823.00 NIST
Ip 820.00 NIST
Ip 810.00 NIST
Ip 827.00 NIST
Ip 827.00 NIST
Ip 828.00 NIST
Ip 825.00 NIST
Ip 811.00 NIST
Ip 816.00 NIST
Ip 820.00 NIST
Ip 816.00 NIST
Ip 832.00 NIST
Ip 814.00 NIST
Ip 845.00 NIST
Ip 798.00 NIST
Ip 825.00 NIST
Ip 814.00 NIST
Ip 823.00 NIST
Ip 821.00 NIST
Ip 846.00 NIST
Ip 805.00 NIST
Ip 820.00 NIST
Ip 810.00 NIST
Ip 810.00 NIST
Ip 822.00 NIST
Ip 810.00 NIST
Ip 822.00 NIST
Ip Outlier 854.00 NIST
Ip 816.00 NIST
Ip 800.00 NIST
Ip 818.00 NIST
Ip 845.00 NIST
Ip 814.00 NIST
Ip 814.00 NIST
Ip Outlier 775.00 NIST
Ip 821.00 NIST
Ip 841.00 NIST
Ip 836.00 NIST
Ip 816.00 NIST
Ip 813.00 NIST
Ip 815.00 NIST
Ip 814.00 NIST
Ip 819.00 NIST
Ip Outlier 788.00 NIST
Ip 823.00 NIST
Ip Outlier 847.00 NIST
Ip 835.00 NIST
Ip 810.00 NIST
Ip 824.00 NIST
Ip 815.00 NIST
Ip 820.00 NIST
Ip 821.00 NIST
Ip 820.00 NIST
Ip 816.00 NIST
Ip 810.00 NIST
Ip Outlier 847.00 NIST
Ip 819.00 NIST
Ip 810.00 NIST
Ip 813.00 NIST
Ip 830.00 NIST
Ip 809.00 NIST
Ip 821.30 NIST
Ip 811.00 NIST
Ip 794.00 NIST
S°liquid [200.00; 220.50] J/mol×K Show Hide
S°liquid 200.40 J/mol×K NIST
S°liquid 200.00 J/mol×K NIST
S°liquid 220.50 J/mol×K NIST
S°liquid 217.60 J/mol×K NIST
Tboil [323.40; 331.15] K Show Hide
Tboil 329.30 K Vapor-liquid equilibrium in the production of the ionic liquid, 1-hexyl-3-methylimidazolium bromide ([HMIm][Br]), in acetone
Tboil 329.26 K Isobaric vapor-liquid equilibrium for acetone + methanol system containing different ionic liquids at 101.3 kPa
Tboil 329.56 K Isobaric vapour-liquid equilibrium measurements and extractive distillation process for the azeotrope of (N,N-dimethylisopropylamine + acetone)
Tboil 329.33 K Isobaric Vapor-Liquid Equilibrium Data for the Acetone + Hexamethyl Disiloxane + Ethyl Acetate Ternary System at 101.3 kPa: Determination and Correlation
Tboil 329.35 K Isobaric Vapor-Liquid Equilibrium of Acetone + Methanol System in the Presence of Calcium Bromide
Tboil 329.27 K Measurement of Isobaric Vapor - Liquid Equilibria of Dimethyl Carbonate with Acetone, 2-Butanone and 2-Pentanone at 101.3 kPa and Density and Speed of Sound at 298.15 K
Tboil 329.37 K Vapor Liquid Equilibrium for the 1,1,1-Trifluorotrichloroethane + Sulfuryl Chloride System at 101.3 kPa
Tboil 329.22 K ChemSep v8.3 pure component data Compiled value
Tboil 329.20 K KDB
Tboil 329.22 K NCMS SOLV-DB
Tboil 329.20 ± 0.20 K NIST
Tboil 329.30 ± 0.20 K NIST
Tboil 329.45 ± 0.15 K NIST
Tboil 329.45 ± 0.30 K NIST
Tboil 329.00 K NIST
Tboil 329.21 ± 0.04 K NIST
Tboil 329.30 K NIST
Tboil 329.45 ± 0.30 K NIST
Tboil 329.40 ± 0.40 K NIST
Tboil 329.25 ± 0.30 K NIST
Tboil 329.47 ± 0.50 K NIST
Tboil 329.23 ± 0.05 K NIST
Tboil 329.25 ± 0.05 K NIST
Tboil 329.26 ± 0.30 K NIST
Tboil 329.00 ± 0.20 K NIST
Tboil 329.30 ± 0.20 K NIST
Tboil 329.30 ± 0.06 K NIST
Tboil 329.25 K NIST
Tboil 329.25 ± 0.15 K NIST
Tboil 329.38 ± 0.30 K NIST
Tboil 329.40 ± 0.20 K NIST
Tboil 329.15 ± 0.30 K NIST
Tboil 329.00 ± 1.00 K NIST
Tboil 329.30 ± 0.20 K NIST
Tboil 329.30 ± 0.30 K NIST
Tboil 329.40 ± 0.40 K NIST
Tboil 329.25 ± 0.50 K NIST
Tboil 329.25 ± 0.30 K NIST
Tboil 329.21 ± 0.10 K NIST
Tboil 329.25 ± 0.30 K NIST
Tboil 329.26 ± 0.30 K NIST
Tboil 329.65 ± 1.00 K NIST
Tboil Outlier 330.95 ± 1.00 K NIST
Tboil 329.25 ± 0.50 K NIST
Tboil 329.26 ± 0.50 K NIST
Tboil 329.15 ± 1.00 K NIST
Tboil Outlier 326.15 ± 1.00 K NIST
Tboil 329.33 ± 0.20 K NIST
Tboil 329.25 ± 1.00 K NIST
Tboil 329.75 ± 1.00 K NIST
Tboil 328.90 ± 0.40 K NIST
Tboil 329.25 ± 0.50 K NIST
Tboil 329.35 ± 1.00 K NIST
Tboil 329.28 ± 0.15 K NIST
Tboil 329.15 ± 1.00 K NIST
Tboil 329.25 ± 0.50 K NIST
Tboil 329.35 ± 0.50 K NIST
Tboil 329.35 ± 0.50 K NIST
Tboil 329.35 ± 0.50 K NIST
Tboil 329.35 ± 0.20 K NIST
Tboil 329.33 ± 0.20 K NIST
Tboil 329.28 ± 0.30 K NIST
Tboil 329.50 ± 0.50 K NIST
Tboil 329.30 ± 0.50 K NIST
Tboil 329.65 ± 0.50 K NIST
Tboil 328.65 ± 1.00 K NIST
Tboil 329.35 ± 0.50 K NIST
Tboil 329.65 ± 1.00 K NIST
Tboil 329.30 ± 0.50 K NIST
Tboil 329.15 ± 1.00 K NIST
Tboil Outlier 323.40 ± 0.30 K NIST
Tboil 329.27 ± 0.50 K NIST
Tboil 329.30 ± 0.50 K NIST
Tboil 329.40 ± 1.00 K NIST
Tboil 329.25 ± 1.00 K NIST
Tboil 330.15 ± 0.50 K NIST
Tboil 329.75 ± 0.50 K NIST
Tboil 329.25 ± 1.00 K NIST
Tboil 329.65 ± 1.00 K NIST
Tboil 329.20 ± 1.00 K NIST
Tboil 329.15 ± 1.00 K NIST
Tboil 329.26 ± 0.10 K NIST
Tboil Outlier 331.15 ± 3.00 K NIST
Tboil 328.85 ± 1.00 K NIST
Tboil 329.15 ± 2.00 K NIST
Tboil 328.57 ± 1.00 K NIST
Tboil 329.30 ± 1.00 K NIST
Tboil 329.55 ± 1.00 K NIST
Tboil 329.65 ± 0.30 K NIST
Tboil 328.75 ± 1.00 K NIST
Tboil 328.95 ± 1.00 K NIST
Tboil 329.40 ± 0.20 K NIST
Tboil 329.39 ± 0.50 K NIST
Tboil 330.00 ± 1.00 K NIST
Tboil 329.35 ± 0.30 K NIST
Tboil 329.35 ± 0.30 K NIST
Tboil 329.45 ± 1.00 K NIST
Tboil 329.35 ± 0.30 K NIST
Tboil 329.25 ± 0.20 K NIST
Tboil 329.30 ± 0.40 K NIST
Tboil 329.35 ± 0.20 K NIST
Tboil 329.17 ± 0.20 K NIST
Tboil 329.50 ± 0.50 K NIST
Tboil 329.32 ± 0.30 K NIST
Tboil 329.65 ± 1.00 K NIST
Tboil 329.15 ± 1.00 K NIST
Tboil 329.35 ± 1.00 K NIST
Tboil 329.22 ± 0.20 K NIST
Tboil 329.23 ± 0.10 K NIST
Tboil 329.30 ± 1.00 K NIST
Tboil 329.20 ± 0.30 K NIST
Tboil 329.48 ± 1.00 K NIST
Tboil 329.25 ± 1.00 K NIST
Tboil 329.65 ± 1.00 K NIST
Tboil 329.35 ± 1.00 K NIST
Tboil 329.45 ± 0.50 K NIST
Tboil 329.65 ± 1.00 K NIST
Tboil 329.30 ± 0.30 K NIST
Tboil 329.15 ± 1.00 K NIST
Tboil 329.65 ± 1.00 K NIST
Tboil 329.70 ± 1.50 K NIST
Tboil 329.30 ± 0.50 K NIST
Tboil 329.40 ± 1.00 K NIST
Tboil 329.25 ± 0.30 K NIST
Tboil 329.30 ± 0.50 K NIST
Tboil 329.30 ± 1.00 K NIST
Tboil 329.25 ± 0.30 K NIST
Tboil 330.20 ± 1.00 K NIST
Tboil 329.34 ± 0.50 K NIST
Tboil 329.15 ± 1.00 K NIST
Tboil 329.40 ± 1.00 K NIST
Tboil 329.55 ± 1.00 K NIST
Tboil 330.15 ± 1.00 K NIST
Tboil 329.55 ± 1.00 K NIST
Tboil 328.90 ± 1.00 K NIST
Tboil 329.50 ± 1.00 K NIST
Tboil 329.50 ± 0.50 K NIST
Tboil Outlier 330.85 ± 1.00 K NIST
Tboil 329.45 ± 1.00 K NIST
Tboil 329.45 ± 1.00 K NIST
Tc [505.80; 509.40] K Show Hide
Tc 508.10 K IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Tc 508.10 K PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc 508.10 K ChemSep v8.3 pure component data Compiled value
Tc 508.10 K KDB
Tc 508.20 K NIST
Tc 508.35 ± 0.40 K NIST
Tc 508.10 ± 0.20 K NIST
Tc 508.10 ± 0.06 K NIST
Tc 508.70 ± 0.70 K NIST
Tc 508.20 ± 0.40 K NIST
Tc 509.10 ± 0.80 K NIST
Tc 508.15 ± 0.20 K NIST
Tc 508.15 ± 0.50 K NIST
Tc 507.70 ± 1.00 K NIST
Tc 509.40 ± 0.39 K NIST
Tc 508.10 ± 0.25 K NIST
Tc 508.70 ± 1.00 K NIST
Tc 509.00 ± 1.00 K NIST
Tc 508.75 ± 0.30 K NIST
Tc 506.90 ± 1.00 K NIST
Tc 507.60 ± 1.00 K NIST
Tc Outlier 505.80 ± 2.00 K NIST
Tc Outlier 506.00 ± 2.00 K NIST
Tfus [177.80; 179.37] K Show Hide
Tfus 178.35 K Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus 178.45 K ChemSep v8.3 pure component data Compiled value
Tfus 178.30 K KDB
Tfus 178.45 K NCMS SOLV-DB
Tfus 179.00 K NIST
Tfus 178.45 K NIST
Tfus 178.25 ± 0.10 K NIST
Tfus 178.10 ± 0.10 K NIST
Tfus 178.55 ± 0.05 K NIST
Tfus 177.80 ± 0.20 K NIST
Tfus 179.37 ± 0.50 K NIST
Tfus 178.60 ± 0.20 K NIST
Tfus 179.15 ± 0.30 K NIST
Tfus 178.85 ± 0.30 K NIST
Tfus 178.85 ± 0.30 K NIST
Tfus 179.00 ± 2.00 K NIST
Ttriple [176.60; 178.50] K Show Hide
Ttriple 176.73 K Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple 178.45 K ChemSep v8.3 pure component data Compiled value
Ttriple 178.50 ± 0.30 K NIST
Ttriple 176.60 ± 0.15 K NIST
Ttriple 177.60 ± 0.30 K NIST
Ttriple 177.60 ± 0.20 K NIST
Ttriple 176.60 ± 0.15 K NIST
Ttriple 177.60 ± 0.30 K NIST
Ttriple 177.60 ± 0.20 K NIST
UQi 2.34 ChemSep v8.3 pure component data Compiled value
URi 2.57 ChemSep v8.3 pure component data Compiled value
Vc [0.209; 0.213] m3/kmol Show Hide
Vc 0.213 m3/kmol IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Vc 0.209 m3/kmol PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc 0.209 m3/kmol ChemSep v8.3 pure component data Compiled value
Vc 0.209 m3/kmol KDB
VCOSTALD 0.21 m3/kmol Hankinson and Thomson (1979), COSTALD parameters Compiled value
ωSRK 0.31 Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zc [0.2325190; 0.2370000]   Show Hide
Zc 0.2370000 IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Zc 0.2330000 ChemSep v8.3 pure component data Compiled value
Zc 0.2325190 KDB
Zra [0.25; 0.25]   Show Hide
Zra 0.25 Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zra 0.25 KDB

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,gas [80.58; 100.50] J/mol×K [332.60; 439.20] Show Hide
Cp,gas 80.58 ± 0.81 J/mol×K 332.60 NIST
Cp,gas 80.96 ± 0.81 J/mol×K 334.00 NIST
Cp,gas 81.50 ± 0.16 J/mol×K 338.20 NIST
Cp,gas 83.35 ± 0.83 J/mol×K 347.80 NIST
Cp,gas 83.39 ± 0.83 J/mol×K 348.00 NIST
Cp,gas 87.03 ± 0.87 J/mol×K 363.00 NIST
Cp,gas 87.19 ± 0.17 J/mol×K 371.20 NIST
Cp,gas 87.53 ± 0.88 J/mol×K 372.30 NIST
Cp,gas 89.24 ± 0.89 J/mol×K 378.00 NIST
Cp,gas 91.84 ± 0.92 J/mol×K 393.00 NIST
Cp,gas 92.93 ± 0.19 J/mol×K 405.20 NIST
Cp,gas 94.18 ± 0.94 J/mol×K 408.00 NIST
Cp,gas 93.30 J/mol×K 410.00 NIST
Cp,gas 96.80 ± 1.90 J/mol×K 422.60 NIST
Cp,gas 99.40 ± 2.00 J/mol×K 428.00 NIST
Cp,gas 100.50 ± 2.00 J/mol×K 438.00 NIST
Cp,gas 98.66 ± 0.20 J/mol×K 439.20 NIST
Cp,liquid [121.30; 133.90] J/mol×K [260.00; 302.40] Show Hide
Cp,liquid 124.30 J/mol×K 260.00 NIST
Cp,liquid 121.30 J/mol×K 283.00 NIST
Cp,liquid 124.70 J/mol×K 289.40 NIST
Cp,liquid 126.30 J/mol×K 293.00 NIST
Cp,liquid 125.90 J/mol×K 293.20 NIST
Cp,liquid 124.68 J/mol×K 296.99 NIST
Cp,liquid 128.24 J/mol×K 298.00 NIST
Cp,liquid 124.70 J/mol×K 298.00 NIST
Cp,liquid 133.90 J/mol×K 298.00 NIST
Cp,liquid 124.70 J/mol×K 298.00 NIST
Cp,liquid 129.70 J/mol×K 298.00 NIST
Cp,liquid 125.45 J/mol×K 298.15 NIST
Cp,liquid 123.80 J/mol×K 298.15 NIST
Cp,liquid 123.80 J/mol×K 298.15 NIST
Cp,liquid 126.60 J/mol×K 298.15 NIST
Cp,liquid 126.60 J/mol×K 298.15 NIST
Cp,liquid 123.80 J/mol×K 298.15 NIST
Cp,liquid 125.90 J/mol×K 298.15 NIST
Cp,liquid 125.56 J/mol×K 298.20 NIST
Cp,liquid 123.80 J/mol×K 298.40 NIST
Cp,liquid 128.40 J/mol×K 302.40 NIST
Cp,solid 96.00 J/mol×K 173.00 NIST
η [0.0002809; 0.0003849] Pa×s [278.15; 313.15] Show Hide
η 0.0003849 Pa×s 278.15 Density and Viscosity of (2,2-Dichloro-N,N-di-2-propenylacetamide + Acetone) and (2,2-Dichloro-N,N-di-2-propenylacetamide + Ethanol) at T = (278.15 to 313.15) K
η 0.0003657 Pa×s 283.15 Density and Viscosity of (2,2-Dichloro-N,N-di-2-propenylacetamide + Acetone) and (2,2-Dichloro-N,N-di-2-propenylacetamide + Ethanol) at T = (278.15 to 313.15) K
η 0.0003511 Pa×s 288.15 Density and Viscosity of (2,2-Dichloro-N,N-di-2-propenylacetamide + Acetone) and (2,2-Dichloro-N,N-di-2-propenylacetamide + Ethanol) at T = (278.15 to 313.15) K
η 0.0003339 Pa×s 293.15 Density and Viscosity of (2,2-Dichloro-N,N-di-2-propenylacetamide + Acetone) and (2,2-Dichloro-N,N-di-2-propenylacetamide + Ethanol) at T = (278.15 to 313.15) K
η 0.0003200 Pa×s 293.15 Dynamic Viscosities of the Binary Systems Cyclohexane and Cyclopentane with Acetone, Butanone, or 2-Pentanone at Three Temperatures T ) (293.15, 298.15, and 303.15) K
η 0.0003200 Pa×s 293.15 Physical properties of the binary systems methylcyclopentane with ketones (acetone, butanone and 2-pentanone) at T = (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO interaction parameters
η 0.0003060 Pa×s 298.15 Physical properties of the binary systems methylcyclopentane with ketones (acetone, butanone and 2-pentanone) at T = (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO interaction parameters
η 0.0003029 Pa×s 298.15 NCMS SOLV-DB
η 0.0003027 Pa×s 298.15 Excess parameter studies on the binary mixtures of toluene with ketones at different temperatures
η 0.0003212 Pa×s 298.15 Density and Viscosity of (2,2-Dichloro-N,N-di-2-propenylacetamide + Acetone) and (2,2-Dichloro-N,N-di-2-propenylacetamide + Ethanol) at T = (278.15 to 313.15) K
η 0.0003060 Pa×s 298.15 Dynamic Viscosities of the Binary Systems Cyclohexane and Cyclopentane with Acetone, Butanone, or 2-Pentanone at Three Temperatures T ) (293.15, 298.15, and 303.15) K
η 0.0003027 Pa×s 298.15 Density and Viscosity of Ketones with Toluene at Different Temperatures and at Atmospheric Pressure
η 0.0002918 Pa×s 303.15 Density and Viscosity of Ketones with Toluene at Different Temperatures and at Atmospheric Pressure
η 0.0002920 Pa×s 303.15 Dynamic Viscosities of the Binary Systems Cyclohexane and Cyclopentane with Acetone, Butanone, or 2-Pentanone at Three Temperatures T ) (293.15, 298.15, and 303.15) K
η 0.0002918 Pa×s 303.15 Excess parameter studies on the binary mixtures of toluene with ketones at different temperatures
η 0.0003086 Pa×s 303.15 Density and Viscosity of (2,2-Dichloro-N,N-di-2-propenylacetamide + Acetone) and (2,2-Dichloro-N,N-di-2-propenylacetamide + Ethanol) at T = (278.15 to 313.15) K
η 0.0002920 Pa×s 303.15 Physical properties of the binary systems methylcyclopentane with ketones (acetone, butanone and 2-pentanone) at T = (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO interaction parameters
η 0.0002809 Pa×s 308.15 Density and Viscosity of Ketones with Toluene at Different Temperatures and at Atmospheric Pressure
η 0.0002809 Pa×s 308.15 Excess parameter studies on the binary mixtures of toluene with ketones at different temperatures
η 0.0002939 Pa×s 308.15 Density and Viscosity of (2,2-Dichloro-N,N-di-2-propenylacetamide + Acetone) and (2,2-Dichloro-N,N-di-2-propenylacetamide + Ethanol) at T = (278.15 to 313.15) K
η 0.0002839 Pa×s 313.15 Density and Viscosity of (2,2-Dichloro-N,N-di-2-propenylacetamide + Acetone) and (2,2-Dichloro-N,N-di-2-propenylacetamide + Ethanol) at T = (278.15 to 313.15) K
ΔfusH [4.77; 5.72] kJ/mol [176.60; 178.50] Show Hide
ΔfusH 5.72 kJ/mol 176.60 NIST
ΔfusH 5.72 kJ/mol 176.60 NIST
ΔfusH 5.71 kJ/mol 176.62 NIST
ΔfusH 5.71 kJ/mol 176.62 NIST
ΔfusH 5.69 kJ/mol 177.60 NIST
ΔfusH 5.69 kJ/mol 177.60 NIST
ΔfusH 5.69 kJ/mol 177.60 NIST
ΔfusH 5.69 kJ/mol 177.60 NIST
ΔfusH 4.77 kJ/mol 178.50 NIST
ΔvapH [9.20; 35.00] kJ/mol [210.50; 498.00] Show Hide
ΔvapH 32.90 kJ/mol 210.50 NIST
ΔvapH 33.80 kJ/mol 236.00 NIST
ΔvapH 30.70 kJ/mol 271.50 NIST
ΔvapH 32.10 kJ/mol 271.50 NIST
ΔvapH 35.00 kJ/mol 271.50 NIST
ΔvapH 32.60 kJ/mol 285.50 NIST
ΔvapH 32.70 kJ/mol 294.50 NIST
ΔvapH 32.80 kJ/mol 305.00 NIST
ΔvapH 31.90 kJ/mol 307.00 NIST
ΔvapH 32.10 kJ/mol 308.00 NIST
ΔvapH 31.80 kJ/mol 319.00 NIST
ΔvapH 31.10 kJ/mol 319.50 NIST
ΔvapH 29.10 kJ/mol 329.30 NIST
ΔvapH 29.12 kJ/mol 329.40 KDB
ΔvapH 29.09 kJ/mol 338.00 NIST
ΔvapH 30.60 kJ/mol 351.00 NIST
ΔvapH 26.10 kJ/mol 373.00 NIST
ΔvapH 29.90 kJ/mol 408.50 NIST
ΔvapH 29.50 kJ/mol 419.00 NIST
ΔvapH 21.70 kJ/mol 423.00 NIST
ΔvapH 15.30 kJ/mol 473.00 NIST
ΔvapH 29.70 kJ/mol 482.50 NIST
ΔvapH 9.20 kJ/mol 498.00 NIST
Pvap [30.23; 302.56] kPa [297.66; 365.43] Show Hide
Pvap 30.23 kPa 297.66 Vapor-Liquid Equilibrium for Binary Systems of Diacetyl with Methanol and Acetone
Pvap 30.23 kPa 297.67 Vapor Liquid Equilibrium for Binary Systems of 2,3-Pentanedione with Diacetyl and Acetone
Pvap 30.80 kPa 298.15 NCMS SOLV-DB
Pvap 35.22 kPa 301.25 Vapor-Liquid Equilibrium for Binary Systems of Diacetyl with Methanol and Acetone
Pvap 35.22 kPa 301.25 Vapor Liquid Equilibrium for Binary Systems of 2,3-Pentanedione with Diacetyl and Acetone
Pvap 38.04 kPa 303.15 Vapor-Liquid Equilibrium for Binary Systems of Diacetyl with Methanol and Acetone
Pvap 40.00 kPa 304.37 Vapor-Liquid Equilibrium for Binary Systems of Diacetyl with Methanol and Acetone
Pvap 45.21 kPa 307.33 Vapor Liquid Equilibrium for Binary Systems of 2,3-Pentanedione with Diacetyl and Acetone
Pvap 45.21 kPa 307.33 Vapor-Liquid Equilibrium for Binary Systems of Diacetyl with Methanol and Acetone
Pvap 50.40 kPa 310.08 Vapor-Liquid Equilibrium for Binary Systems of Diacetyl with Methanol and Acetone
Pvap 50.40 kPa 310.08 Vapor Liquid Equilibrium for Binary Systems of 2,3-Pentanedione with Diacetyl and Acetone
Pvap 55.29 kPa 312.52 Vapor Liquid Equilibrium for Binary Systems of 2,3-Pentanedione with Diacetyl and Acetone
Pvap 55.29 kPa 312.52 Vapor-Liquid Equilibrium for Binary Systems of Diacetyl with Methanol and Acetone
Pvap 56.64 kPa 313.15 Vapor-Liquid Equilibrium for Binary Systems of Diacetyl with Methanol and Acetone
Pvap 57.96 kPa 314.00 Isobaric vapor liquid equilibria for acetone + methanol + lithium nitrate at 100 kPa
Pvap 60.29 kPa 314.76 Vapor-Liquid Equilibrium for Binary Systems of Diacetyl with Methanol and Acetone
Pvap 60.29 kPa 314.76 Vapor Liquid Equilibrium for Binary Systems of 2,3-Pentanedione with Diacetyl and Acetone
Pvap 65.08 kPa 316.80 Vapor-Liquid Equilibrium for Binary Systems of Diacetyl with Methanol and Acetone
Pvap 65.08 kPa 316.80 Vapor Liquid Equilibrium for Binary Systems of 2,3-Pentanedione with Diacetyl and Acetone
Pvap 64.95 kPa 317.00 Isobaric vapor liquid equilibria for acetone + methanol + lithium nitrate at 100 kPa
Pvap 68.20 kPa 318.15 Isothermal Vapor-Liquid Equilibria for Binary Mixtures of Methyl Nonafluorobutyl Ether + Acetone, Cyclopentyl Methyl Ether, Ethyl Acetate, n-Heptane, Methanol, and Toluene
Pvap 70.07 kPa 318.77 Vapor-Liquid Equilibrium for Binary Systems of Diacetyl with Methanol and Acetone
Pvap 70.07 kPa 318.77 Vapor Liquid Equilibrium for Binary Systems of 2,3-Pentanedione with Diacetyl and Acetone
Pvap 72.60 kPa 320.00 Isobaric vapor liquid equilibria for acetone + methanol + lithium nitrate at 100 kPa
Pvap 80.96 kPa 323.00 Isobaric vapor liquid equilibria for acetone + methanol + lithium nitrate at 100 kPa
Pvap 81.65 kPa 323.15 Vapor-Liquid Equilibrium for Binary Systems of Diacetyl with Methanol and Acetone
Pvap 90.08 kPa 326.00 Isobaric vapor liquid equilibria for acetone + methanol + lithium nitrate at 100 kPa
Pvap 96.15 kPa 327.90 Vapor Liquid Equilibrium Data for Binary Mixtures of Acetic Acid + Anisole, Acetone + Anisole, and Isopropanol + Anisole at Pressure 96.15 kPa
Pvap 100.00 kPa 329.00 1-Ethyl-3-methylimidazolium Dicyanamide as a Very Efficient Entrainer for the Extractive Distillation of the Acetone + Methanol System
Pvap 100.00 kPa 329.00 Isobaric vapor liquid equilibria for acetone + methanol + lithium nitrate at 100 kPa
Pvap 100.00 kPa 329.00 Influence of Some Ionic Liquids Containing the Trifluoromethanesulfonate Anion on the Vapor Liquid Equilibria of the Acetone + Methanol System
Pvap 101.30 kPa 329.26 Isobaric vapor-liquid equilibrium for acetone + methanol system containing different ionic liquids at 101.3 kPa
Pvap 101.33 kPa 329.30 Vapor-liquid equilibrium in the production of the ionic liquid, 1-hexyl-3-methylimidazolium bromide ([HMIm][Br]), in acetone
Pvap 101.30 kPa 329.33 Isobaric Vapor-Liquid Equilibrium Data for the Acetone + Hexamethyl Disiloxane + Ethyl Acetate Ternary System at 101.3 kPa: Determination and Correlation
Pvap 101.00 kPa 329.35 Isobaric Vapor-Liquid Equilibrium of Acetone + Methanol System in the Presence of Calcium Bromide
Pvap 101.30 kPa 329.37 Vapor Liquid Equilibrium for the 1,1,1-Trifluorotrichloroethane + Sulfuryl Chloride System at 101.3 kPa
Pvap 101.30 kPa 329.56 Isobaric vapour-liquid equilibrium measurements and extractive distillation process for the azeotrope of (N,N-dimethylisopropylamine + acetone)
Pvap 110.78 kPa 332.00 Isobaric vapor liquid equilibria for acetone + methanol + lithium nitrate at 100 kPa
Pvap 115.70 kPa 333.15 Thermodynamics of binary mixtures of N-methyl-2-pyrrolidinone and ketone. Experimental results and modelling of the solid-liquid equilibrium and vapou-liquid equilibrium. The Modified UNIFAC (Do) model characterization
Pvap 122.47 kPa 335.00 Isobaric vapor liquid equilibria for acetone + methanol + lithium nitrate at 100 kPa
Pvap 135.11 kPa 338.00 Isobaric vapor liquid equilibria for acetone + methanol + lithium nitrate at 100 kPa
Pvap 297.10 kPa 364.51 Vapor Liquid Equilibrium for Six Binary Systems of C4-Hydrocarbons + 2-Propanone
Pvap 294.30 kPa 364.51 Vapor Liquid Equilibrium for Six Binary Systems of C4-Hydrocarbons + 2-Propanone
Pvap 296.40 kPa 364.51 Vapor Liquid Equilibrium for Six Binary Systems of C4-Hydrocarbons + 2-Propanone
Pvap 296.80 kPa 364.52 Vapor Liquid Equilibrium for Six Binary Systems of C4-Hydrocarbons + 2-Propanone
Pvap 302.56 kPa 365.43 Vapor Liquid Equilibrium for Six Binary Systems of C4-Hydrocarbons + 2-Propanone
n0 [1.34491; 1.36152]   [288.15; 318.15] Show Hide
n0 1.36146 288.15 Density, Speed of Sound, and Refractive Index of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate with Acetone, Methyl Acetate, and Ethyl Acetate at Temperatures from (278.15 to 328.15) K
n0 1.36152 288.15 Densities, Refractive indices and Viscosities for Binary and Ternary Mixtures of Acetone, Ethanol and 2,2,4-Trimethylpentane at T = (288.15, 298.15, and 308.15) K
n0 1.35860 293.15 Isobaric Vapor Liquid Equilibrium for Nine Binary Systems of Cracking C5 Fraction at 250 kPa
n0 1.35900 293.15 Solubilities of (2,5-Dihydroxyphenyl)diphenyl Phosphine Oxide in Selected Solvents
n0 1.35880 293.15 Isothermal vapour-liquid equilibrium data for the binary systems 2-propanone + (2-butanol or propanoic acid)
n0 1.35900 293.15 Solubilities of 3,9-Dimethyl-3,9-dioxide-2,4,8,10-tetraoxa-3,9-diphosphaspiro[5.5]undecane in Selected Solvents
n0 1.35880 293.15 Solubilities of Methyldiphenylphosphine Oxide in Selected Solvents
n0 1.35900 293.15 Solubilities of 2-(6-Oxido-6H-dibenz[c,e][1,2]oxaphosphorin-6-yl)-1,4-dihydroxy Phenylene in the Selected Solvents
n0 1.35900 293.15 Solubilities of Phosphorus-Containing Compounds in Selected Solvents
n0 1.35900 293.15 Solubilities of Some Phosphaspirocyclic Compounds in Selected Solvents
n0 1.35890 293.15 Isothermal and Isobaric Vapor-Liquid Equilibria of the Ternary System of 2,2-Dimethoxypropane + Acetone + Methanol
n0 1.35550 298.00 Quaternary and ternary LLE measurements for solvent (2-methyltetrahydrofuran and cyclopentyl methyl ether) + furfural + acetic acid + water between 298 and 343 K
n0 1.35600 298.15 Physical properties and their corresponding changes of mixing for the ternary mixture acetone + n-hexane +water at 298.15K
n0 1.35566 298.15 Properties of ionic liquid HMIMPF6 with carbonates, ketones and alkyl acetates
n0 1.35553 298.15 Quaternary, Ternary, and Binary LLE Measurements for 2-Methoxy-2-methylpropane + Furfural + Acetic Acid + Water at Temperatures between 298 and 307 K
n0 1.35553 298.15 Ternary and Binary LLE Measurements for Solvent (4- Methyl-2-pentanone and 2-Methyl-2-butanol) + Furfural + Water between 298 and 401 K
n0 1.35605 298.15 Densities, Refractive indices and Viscosities for Binary and Ternary Mixtures of Acetone, Ethanol and 2,2,4-Trimethylpentane at T = (288.15, 298.15, and 308.15) K
n0 1.35500 298.15 NCMS SOLV-DB
n0 1.35630 298.15 Water as a solute in aprotic dipolar solvents. 1. D2O-H2O solute isotope effects on the enthalpy of water dissolution in acetone, tetrahydrofuran and 1,4-dioxane at 298.15 K
n0 1.35630 298.15 Enthalpies of solution of tetramethyl-bis-urea (Mebicarum) in amides and acetone at 298.15 K
n0 1.35620 298.15 Solubility of a-Carotene in Binary Solvents Formed by Some Hydrocarbons with 2,5,8-Trioxanonane, 2-Propanone, and Cyclohexanone
n0 1.35597 298.15 Isobaric vapor liquid equilibria for mixtures of acetone, ethanol, and 2,2,4-trimethylpentane at 101.3 kPa
n0 1.35550 298.15 Ternary and binary LLE measurements for solvent (2-methyltetrahydrofuran and cyclopentyl methyl ether) + furfural + water between 298 and 343 K
n0 1.35820 298.15 Isobaric Vapor Liquid Equilibria for Binary Systems of Acetone + Isopropenyl Acetate, 2-Butanone + Isopropenyl Acetate, and Isopropenyl Acetate + Acetylacetone at 101.3 kPa
n0 1.35640 298.15 Enthalpies of solution of N,N,N0,N0-tetramethylurea in amides, dimethylsulphoxide, and acetone at 298.15 K
n0 1.35553 298.15 Quaternary, Ternary and Binary LLE Measurements for 2-Methoxy-2-methylbutane + Furfural + Acetic Acid + Water at Temperatures between 298 and 341 K
n0 1.35732 298.15 Phase equilibria and interfacial tensions in the systems methyl tert-butyl ether + acetone + cyclohexane, methyl tert-butyl ether + acetone and methyl tert-butyl ether + cyclohexane
n0 1.35597 298.15 Density, Speed of Sound, and Refractive Index of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate with Acetone, Methyl Acetate, and Ethyl Acetate at Temperatures from (278.15 to 328.15) K
n0 1.35732 298.15 Vapor liquid equilibria and interfacial tensions for the ternary system acetone + 2,2 -oxybis[propane] + cyclohexane and its constituent binary systems
n0 1.35054 308.15 Density, Speed of Sound, and Refractive Index of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate with Acetone, Methyl Acetate, and Ethyl Acetate at Temperatures from (278.15 to 328.15) K
n0 1.35057 308.15 Densities, Refractive indices and Viscosities for Binary and Ternary Mixtures of Acetone, Ethanol and 2,2,4-Trimethylpentane at T = (288.15, 298.15, and 308.15) K
n0 1.34491 318.15 Density, Speed of Sound, and Refractive Index of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate with Acetone, Methyl Acetate, and Ethyl Acetate at Temperatures from (278.15 to 328.15) K
ρl [755.31; 801.67] kg/m3 [283.15; 323.14] Show Hide
ρl 801.67 kg/m3 283.15 Experimental Densities and Excess Volumes for Binary Mixtures Containing Propionic Acid, Acetone and Water from 283.15 K to 323.15 K at Atmospheric Pressure
ρl 796.04 kg/m3 288.15 Experimental Densities and Excess Volumes for Binary Mixtures Containing Propionic Acid, Acetone and Water from 283.15 K to 323.15 K at Atmospheric Pressure
ρl 790.00 kg/m3 293.00 KDB
ρl 790.36 kg/m3 293.15 Experimental Densities and Excess Volumes for Binary Mixtures Containing Propionic Acid, Acetone and Water from 283.15 K to 323.15 K at Atmospheric Pressure
ρl 784.30 kg/m3 293.15 Liquid Liquid Equilibrium for the Ternary System Acetone Oxime Methyl Ether Acetone Water
ρl 790.21 kg/m3 293.15 (Liquid + liquid) equilibria for (water + 1-propanol or acetone + .beta.-citronellol) at different temperatures
ρl 789.99 kg/m3 293.15 Thermodynamic properties of binary mixtures of the ionic liquid [emim][BF4] with acetone and dimethylsulphoxide
ρl 790.31 kg/m3 293.15 Excess Molar Enthalpies for Binary Mixtures of Ethanol + Acetone, + Octane, + Cyclohexane and 1-Propanol + Acetone, + Octane, + Heptane at 323.15
ρl 790.00 kg/m3 293.15 Thermophysical approach to understand the nature of molecular interactions and structural factor between methyl isobutyl ketone and organic solvents mixtures
ρl 784.50 kg/m3 293.15 (Vapour + liquid) equilibria for (2-ethoxypropene + acetone) and (2-ethoxypropene + butanone)
ρl 790.19 kg/m3 293.15 Thermodynamics of amide + ketone mixtures. 1. Volumetric, speed of sound and refractive index data for N,N-dimethylformamide + 2-alkanone systems at several temperatures
ρl 790.66 kg/m3 293.20 Ionic liquid 1-hexyl-3-methylimidazolium hexafluorophosphate, an efficient solvent for extraction of acetone from aqueous solutions
ρl 784.64 kg/m3 298.15 Experimental Densities and Excess Volumes for Binary Mixtures Containing Propionic Acid, Acetone and Water from 283.15 K to 323.15 K at Atmospheric Pressure
ρl 786.77 kg/m3 298.15 Separation of ethylbenzene/styrene systems using ionic liquids in ternary LLE
ρl 784.43 kg/m3 298.15 Thermodynamics of amide + ketone mixtures. 1. Volumetric, speed of sound and refractive index data for N,N-dimethylformamide + 2-alkanone systems at several temperatures
ρl 785.32 kg/m3 298.15 Effect of the alkyl side chain of the 1-alkylpiperidinium-based ionic liquids on desulfurization of fuels
ρl 785.32 kg/m3 298.15 Extraction desulfurization process of fuels with ionic liquids
ρl 783.80 kg/m3 298.15 Solubility and solution thermodynamics of sorbic acid in eight pure organic solvents
ρl 785.09 kg/m3 298.15 Thermodynamics of ketone + amine mixtures. Part IX. Excess molar enthalpies at 298.15K for dipropylamine, or dibutylamine + 2-alkanone systems and modeling of linear or aromatic amine + 2-alkanone mixtures in terms of DISQUAC and ERAS
ρl 783.81 kg/m3 298.15 Partial Molar Volumes of Butyltriethylammonium Iodide in Single Nonaqueous Solvents at 298.15 K
ρl 784.41 kg/m3 298.15 Densities, viscosities, and refractive indices of binary and ternary mixtures of methanol, acetone, and chloroform at temperatures from (298.15-318.15) K and ambient pressure
ρl 784.10 kg/m3 298.15 Density, Speed of Sound, and Derived Thermodynamic Properties of Ionic Liquids [EMIM]+[BETI]- or ([EMIM]+[CH3(OCH2CH2)2OSO3]- + Methanol or + Acetone) at T = (298.15 or 303.15 or 313.15) K
ρl 785.10 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 785.23 kg/m3 298.15 Separation of sulfur compounds from alkanes with 1-alkylcyanopyridinium-based ionic liquids
ρl 785.23 kg/m3 298.15 Separation of pyridine from heptane with tricyanomethanide-based ionic liquids
ρl 784.30 kg/m3 298.15 Phase equilibrium study of binary and ternary mixtures of ionic liquids + acetone + methanol
ρl 785.09 kg/m3 298.15 Thermodynamics of ketone + amine mixtures. Part X. Excess molarenthalpies at 298.15 K for N,N,N-triethylamine + 2-alkanone systems.Characterization of tertiary amine + 2-alkanone, and ofamino-ketone + n-alkane mixtures in terms of DISQUAC
ρl 784.40 kg/m3 298.15 Thermodynamic properties of binary mixtures of the ionic liquid [emim][BF4] with acetone and dimethylsulphoxide
ρl 785.09 kg/m3 298.15 Thermodynamics of Ketone + Amine Mixtures. Part VIII. Molar Excess Enthalpies at 298.15 K for n-Alkanone + Aniline or + N-Methylaniline Systems
ρl 784.39 kg/m3 298.15 Excess Molar Volumes and Surface Tensions of Xylene with Acetone or 2-Butanone at 298.15 K
ρl 784.65 kg/m3 298.15 Excess molar enthalpies and volumes of binary mixtures of nonafluorobutylmethylether with ketones at T = 298.15 K
ρl 784.42 kg/m3 298.15 Dielectric study of H-bonded interactions in amyl alcohols with ketones and DMSO at T = 298.15 K
ρl 785.00 kg/m3 298.15 Vapor Liquid Equilibrium Data for 2,3-Pentanedione + (Acetaldehyde or Acetone) at (100, 150, and 200) kPa
ρl 784.24 kg/m3 298.15 Apparent molar volumes and compressibilities of tetrabutyl-ammonium bromide in organic solvents
ρl 784.23 kg/m3 298.15 Density and speed of sound of lithium bromide with organic solvents: Measurement and correlation
ρl 784.40 kg/m3 298.20 Ionic liquid 1-hexyl-3-methylimidazolium hexafluorophosphate, an efficient solvent for extraction of acetone from aqueous solutions
ρl 778.88 kg/m3 303.14 Experimental Densities and Excess Volumes for Binary Mixtures Containing Propionic Acid, Acetone and Water from 283.15 K to 323.15 K at Atmospheric Pressure
ρl 778.87 kg/m3 303.15 Thermodynamic properties of binary mixtures of the ionic liquid [emim][BF4] with acetone and dimethylsulphoxide
ρl 778.63 kg/m3 303.15 Thermodynamics of amide + ketone mixtures. 1. Volumetric, speed of sound and refractive index data for N,N-dimethylformamide + 2-alkanone systems at several temperatures
ρl 778.40 kg/m3 303.15 Density, Speed of Sound, and Derived Thermodynamic Properties of Ionic Liquids [EMIM]+[BETI]- or ([EMIM]+[CH3(OCH2CH2)2OSO3]- + Methanol or + Acetone) at T = (298.15 or 303.15 or 313.15) K
ρl 779.00 kg/m3 303.15 Thermophysical approach to understand the nature of molecular interactions and structural factor between methyl isobutyl ketone and organic solvents mixtures
ρl 778.66 kg/m3 303.15 Densities, viscosities, and refractive indices of binary and ternary mixtures of methanol, acetone, and chloroform at temperatures from (298.15-318.15) K and ambient pressure
ρl 778.70 kg/m3 303.20 Ionic liquid 1-hexyl-3-methylimidazolium hexafluorophosphate, an efficient solvent for extraction of acetone from aqueous solutions
ρl 773.07 kg/m3 308.15 Experimental Densities and Excess Volumes for Binary Mixtures Containing Propionic Acid, Acetone and Water from 283.15 K to 323.15 K at Atmospheric Pressure
ρl 773.07 kg/m3 308.15 Thermodynamic properties of binary mixtures of the ionic liquid [emim][BF4] with acetone and dimethylsulphoxide
ρl 773.08 kg/m3 308.15 Densities, viscosities, and refractive indices of binary and ternary mixtures of methanol, acetone, and chloroform at temperatures from (298.15-318.15) K and ambient pressure
ρl 767.21 kg/m3 313.14 Experimental Densities and Excess Volumes for Binary Mixtures Containing Propionic Acid, Acetone and Water from 283.15 K to 323.15 K at Atmospheric Pressure
ρl 766.95 kg/m3 313.15 Densities, viscosities, and refractive indices of binary and ternary mixtures of methanol, acetone, and chloroform at temperatures from (298.15-318.15) K and ambient pressure
ρl 767.00 kg/m3 313.15 Thermophysical approach to understand the nature of molecular interactions and structural factor between methyl isobutyl ketone and organic solvents mixtures
ρl 766.90 kg/m3 313.15 Density, Speed of Sound, and Derived Thermodynamic Properties of Ionic Liquids [EMIM]+[BETI]- or ([EMIM]+[CH3(OCH2CH2)2OSO3]- + Methanol or + Acetone) at T = (298.15 or 303.15 or 313.15) K
ρl 761.29 kg/m3 318.14 Experimental Densities and Excess Volumes for Binary Mixtures Containing Propionic Acid, Acetone and Water from 283.15 K to 323.15 K at Atmospheric Pressure
ρl 761.26 kg/m3 318.15 Densities, viscosities, and refractive indices of binary and ternary mixtures of methanol, acetone, and chloroform at temperatures from (298.15-318.15) K and ambient pressure
ρl 755.31 kg/m3 323.14 Experimental Densities and Excess Volumes for Binary Mixtures Containing Propionic Acid, Acetone and Water from 283.15 K to 323.15 K at Atmospheric Pressure
ΔfusS [26.70; 32.36] J/mol×K [176.62; 178.50] Show Hide
ΔfusS 32.36 J/mol×K 176.62 NIST
ΔfusS 32.36 J/mol×K 176.62 NIST
ΔfusS 32.00 J/mol×K 177.60 NIST
ΔfusS 32.03 J/mol×K 177.60 NIST
ΔfusS 32.00 J/mol×K 177.60 NIST
ΔfusS 32.03 J/mol×K 177.60 NIST
ΔfusS 26.70 J/mol×K 178.50 NIST
csound,fluid [1138.70; 1182.80] m/s [293.15; 303.15] Show Hide
csound,fluid 1182.80 m/s 293.15 Thermodynamics of Ketone + Amine Mixtures. I. Volumetric and Speed of Sound Data at (293.15, 298.15, and 303.15) K for 2-Propanone + Aniline, + N-Methylaniline, or + Pyridine Systems
csound,fluid 1162.00 m/s 298.15 Vapor liquid equilibria for systems of diethyl carbonate and ketones and determination of group interaction parameters for the UNIFAC and ASOG methods
csound,fluid 1160.70 m/s 298.15 Thermodynamics of Ketone + Amine Mixtures. I. Volumetric and Speed of Sound Data at (293.15, 298.15, and 303.15) K for 2-Propanone + Aniline, + N-Methylaniline, or + Pyridine Systems
csound,fluid 1138.70 m/s 303.15 Thermodynamics of Ketone + Amine Mixtures. I. Volumetric and Speed of Sound Data at (293.15, 298.15, and 303.15) K for 2-Propanone + Aniline, + N-Methylaniline, or + Pyridine Systems
γ [0.02; 0.02] N/m [287.81; 328.15] Show Hide
γ 0.02 N/m 287.81 Surface Tension of Pure Liquids and Binary Liquid Mixtures
γ 0.02 N/m 288.15 Surface Tension of the Ternary System Water + Acetone + Toluene
γ 0.02 N/m 293.15 Investigation of Surface Properties and Solubility of 1-Vinyl-3-alkyl/Esterimidazolium Halide Ionic Liquids by Density Functional Methods
γ 0.02 N/m 297.82 Surface Tension of Pure Liquids and Binary Liquid Mixtures
γ 0.02 N/m 298.15 NCMS SOLV-DB
γ 0.02 N/m 298.15 Surface Tension of the Ternary System Water + Acetone + Toluene
γ 0.02 N/m 298.20 KDB
γ 0.02 N/m 307.86 Surface Tension of Pure Liquids and Binary Liquid Mixtures
γ 0.02 N/m 308.15 Surface Tension of the Ternary System Water + Acetone + Toluene
γ 0.02 N/m 317.86 Surface Tension of Pure Liquids and Binary Liquid Mixtures
γ 0.02 N/m 318.15 Surface Tension of the Ternary System Water + Acetone + Toluene
γ 0.02 N/m 327.88 Surface Tension of Pure Liquids and Binary Liquid Mixtures
γ 0.02 N/m 328.15 Surface Tension of the Ternary System Water + Acetone + Toluene

Pressure Dependent Properties

Property Value Unit Pressure (kPa) Source
Tboilr 329.30 K 2.70 NIST

Datasets

  1. Viscosity, Pa*s (1)
  2. Speed of sound, m/s (2)

Viscosity, Pa*s

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Viscosity, Pa*s - Liquid
303.15 101.30 0.0003
Reference

Speed of sound, m/s

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Speed of sound, m/s - Liquid
265.67 102.00 1298.93
265.67 504.00 1301.09
265.67 750.00 1302.5
265.67 1003.00 1303.56
265.67 1255.00 1304.92
265.67 1501.00 1306.29
265.67 2007.00 1308.73
265.67 2506.00 1311.28
265.67 3005.00 1313.79
265.67 4004.00 1318.59
265.67 5004.00 1323.31
265.67 6005.00 1328.01
265.67 8002.00 1338.69
265.67 10001.00 1349.81
265.67 12001.00 1358.7
265.67 14003.00 1366.48
265.67 16050.00 1375.48
265.67 18001.00 1384.77
265.67 20003.00 1394.13
265.67 23001.00 1407.08
265.67 27004.00 1425.32
265.67 31003.00 1439.78
265.67 34997.00 1455.17
265.67 39999.00 1476.05
265.67 45002.00 1494.61
265.67 49999.00 1511.6
265.67 55001.00 1528.77
265.67 60002.00 1548.05
265.67 65000.00 1564.17
265.67 18001.00 1384.54
273.16 102.00 1264.48
273.16 504.00 1266.57
273.16 750.00 1267.96
273.16 1003.00 1269.39
273.16 1255.00 1270.74
273.16 1501.00 1272.23
273.16 2007.00 1275.12
273.16 2506.00 1277.93
273.16 3005.00 1281.1
273.16 4004.00 1287.23
273.16 5004.00 1291.97
273.16 6005.00 1296.6
273.16 8002.00 1306.58
273.16 10001.00 1316.19
273.16 12001.00 1325.58
273.16 14003.00 1335.9
273.16 16005.00 1346.87
273.16 18001.00 1355.99
273.16 20003.00 1363.63
273.16 23001.00 1376.52
273.16 27004.00 1394.61
273.16 31003.00 1412.24
273.16 34997.00 1428.86
273.16 39999.00 1446.67
273.16 45002.00 1467.44
273.16 49999.00 1485.84
273.16 55001.00 1504.31
273.16 60002.00 1520.08
273.16 65000.00 1538.71
273.16 3005.00 1281.19
273.16 4004.00 1286.78
273.16 5004.00 1292.02
280.74 75.00 1233.63
280.74 504.00 1234.94
280.74 750.00 1236.39
280.74 1003.00 1237.85
280.74 1255.00 1239.22
280.74 1501.00 1240.59
280.74 2007.00 1243.75
280.74 2506.00 1247.03
280.74 3005.00 1249.76
280.74 4004.00 1255.13
280.74 5004.00 1259.87
280.74 6005.00 1264.8
280.74 8002.00 1275.79
280.74 10001.00 1286.82
280.74 12001.00 1296.79
280.74 14003.00 1306.71
280.74 16005.00 1316.23
280.74 18001.00 1325.46
280.74 20003.00 1335.09
280.74 23001.00 1350.8
280.74 27004.00 1366.99
280.74 31003.00 1384.26
280.74 34997.00 1401.32
280.74 39999.00 1423.56
280.74 45002.00 1441.37
280.74 49999.00 1461.28
280.74 55001.00 1480.44
280.74 60002.00 1498.97
280.74 65000.00 1514.56
280.74 75.00 1232.04
280.74 23001.00 1350.8
280.74 39999.00 1423.74
280.74 45002.00 1441.37
280.74 60002.00 1498.91
280.74 65000.00 1514.63
288.23 109.00 1199.01
288.23 504.00 1201.24
288.23 750.00 1202.57
288.23 1003.00 1204.2
288.23 1255.00 1205.54
288.23 1501.00 1206.97
288.23 2007.00 1209.92
288.23 2506.00 1212.8
288.23 3005.00 1215.61
288.23 4004.00 1221.35
288.23 5004.00 1227.14
288.23 6005.00 1232.71
288.23 8002.00 1244.39
288.23 10001.00 1255.4
288.23 12001.00 1265.22
288.23 14003.00 1275.63
288.23 16005.00 1286.61
288.23 18001.00 1296.18
288.23 20003.00 1305.89
288.23 23001.00 1319.61
288.23 27004.00 1339.05
288.23 31003.00 1357.37
288.23 34997.00 1373.83
288.23 39999.00 1395.08
288.23 45002.00 1416.1
288.23 49999.00 1435.37
288.23 55001.00 1453.97
288.23 60002.00 1473.72
288.23 65000.00 1492.08
298.23 109.00 1153.69
298.23 504.00 1156.23
298.23 750.00 1157.82
298.23 1003.00 1159.5
298.23 1255.00 1161.14
298.23 1501.00 1162.71
298.23 2007.00 1165.65
298.23 2506.00 1168.6
298.23 3005.00 1171.49
298.23 4004.00 1177.4
298.23 5004.00 1182.9
298.23 6005.00 1189.6
298.23 8002.00 1201.45
298.23 10001.00 1212.8
298.23 12001.00 1223.83
298.23 14003.00 1234.83
298.23 16005.00 1246.18
298.23 18001.00 1256.46
298.23 20003.00 1265.92
298.23 23001.00 1281.93
298.23 27004.00 1301.17
298.23 31003.00 1319.28
298.23 34997.00 1337.9
298.23 39999.00 1359.25
298.23 45002.00 1380.44
298.23 49999.00 1400.61
298.23 55001.00 1421.32
298.23 60002.00 1439.68
298.23 65000.00 1458.59
308.22 109.00 1107.74
308.22 504.00 1110.52
308.22 750.00 1112.35
308.22 1003.00 1114.01
308.22 1255.00 1115.75
308.22 1501.00 1117.34
308.22 2007.00 1120.69
308.22 2506.00 1123.91
308.22 3005.00 1127.11
308.22 4004.00 1133.79
308.22 5004.00 1140.56
308.22 6005.00 1146.98
308.22 8002.00 1159.51
308.22 10001.00 1171.13
308.22 12001.00 1182.37
308.22 14003.00 1194.75
308.22 16005.00 1205.76
308.22 18001.00 1216.57
308.22 20003.00 1227.49
308.22 23001.00 1244.05
308.22 27004.00 1263.44
308.22 31003.00 1283.97
308.22 34997.00 1302.46
308.22 39999.00 1324.45
308.22 45002.00 1347.09
308.22 49999.00 1367.79
308.22 55001.00 1388.31
308.22 60002.00 1408.07
308.22 65000.00 1427.73
318.22 109.00 1062.32
318.22 504.00 1065.38
318.22 750.00 1067.34
318.22 1003.00 1069.21
318.22 1255.00 1071.11
318.22 1501.00 1072.72
318.22 2007.00 1076.32
318.22 2506.00 1079.71
318.22 3005.00 1083.5
318.22 4004.00 1090.38
318.22 5004.00 1096.85
318.22 6005.00 1103.61
318.22 8002.00 1116.61
318.22 10001.00 1129.13
318.22 12001.00 1142.47
318.22 14003.00 1154.62
318.22 16005.00 1166.43
318.22 18001.00 1177.61
318.22 20003.00 1189.14
318.22 23001.00 1205.63
318.22 27004.00 1226.77
318.22 31003.00 1247.41
318.22 34997.00 1266.28
318.22 39999.00 1290.76
318.22 45002.00 1313.78
318.22 49999.00 1334.83
318.22 55001.00 1356.46
318.22 60002.00 1376.77
318.22 65000.00 1395.43
328.22 129.00 1018.3
328.22 504.00 1021.14
328.22 750.00 1023.1
328.22 1003.00 1024.91
328.22 1255.00 1026.82
328.22 1501.00 1028.6
328.22 2007.00 1032.33
328.22 2506.00 1036.21
328.22 3005.00 1040.05
328.22 4004.00 1047.07
328.22 5004.00 1053.76
328.22 6005.00 1060.7
328.22 8002.00 1074.73
328.22 10001.00 1088.42
328.22 12001.00 1101.14
328.22 14003.00 1113.97
328.22 16005.00 1126.49
328.22 18001.00 1138.92
328.22 20003.00 1151.08
328.22 23001.00 1168.1
328.22 27004.00 1190.45
328.22 31003.00 1211.66
328.22 34997.00 1231.66
328.22 39999.00 1256.67
328.22 45002.00 1280.63
328.22 49999.00 1303.34
328.22 55001.00 1324.67
328.22 60002.00 1345.81
328.22 65000.00 1365.57
338.22 170.00 972.8
338.22 504.00 976.32
338.22 750.00 978.88
338.22 1003.00 981.05
338.22 1255.00 982.97
338.22 1501.00 984.75
338.22 2007.00 988.42
338.22 2506.00 992.07
338.22 3005.00 996.0
338.22 4004.00 1004.26
338.22 5004.00 1011.63
338.22 6005.00 1019.16
338.22 8002.00 1033.34
338.22 10001.00 1047.72
338.22 12001.00 1061.19
338.22 14003.00 1074.71
338.22 16005.00 1088.09
338.22 18001.00 1100.33
338.22 20003.00 1112.58
338.22 23001.00 1131.02
338.22 27004.00 1154.76
338.22 31003.00 1176.19
338.22 34997.00 1197.57
338.22 39999.00 1223.29
338.22 45002.00 1248.14
338.22 49999.00 1271.19
338.22 55001.00 1293.31
338.22 60002.00 1315.39
338.22 65000.00 1336.38
Reference
Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Speed of sound, m/s - Liquid
248.15 100.00 1390.16
248.15 10000.00 1435.51
248.15 20000.00 1478.36
248.15 30000.00 1518.03
248.15 40000.00 1550.78
248.15 50000.00 1590.88
248.15 60000.00 1625.12
248.15 70000.00 1657.38
248.15 80000.00 1688.07
248.15 90000.00 1717.48
248.15 100000.00 1745.43
253.15 100.00 1367.16
253.15 10000.00 1413.84
253.15 20000.00 1457.41
253.15 30000.00 1497.98
253.15 40000.00 1536.44
253.15 50000.00 1572.26
253.15 60000.00 1606.9
253.15 70000.00 1639.52
253.15 80000.00 1670.88
253.15 90000.00 1700.93
253.15 100000.00 1729.65
258.15 100.00 1344.2
258.15 10000.00 1391.98
258.15 20000.00 1436.58
258.15 30000.00 1478.11
258.15 40000.00 1517.33
258.15 50000.00 1553.89
258.15 60000.00 1588.88
258.15 70000.00 1621.91
258.15 80000.00 1653.89
258.15 90000.00 1684.43
258.15 100000.00 1713.62
263.15 100.00 1320.92
263.15 10000.00 1370.35
263.15 20000.00 1415.99
263.15 30000.00 1458.25
263.15 40000.00 1498.44
263.15 50000.00 1535.81
263.15 60000.00 1570.98
263.15 70000.00 1604.54
263.15 80000.00 1637.11
263.15 90000.00 1668.1
263.15 100000.00 1697.74
268.15 100.00 1298.67
268.15 10000.00 1349.08
268.15 20000.00 1395.62
268.15 30000.00 1438.54
268.15 40000.00 1479.77
268.15 50000.00 1517.83
268.15 60000.00 1553.2
268.15 70000.00 1587.43
268.15 80000.00 1620.54
268.15 90000.00 1651.96
268.15 100000.00 1682.01
273.15 100.00 1275.4
273.15 10000.00 1327.81
273.15 20000.00 1375.45
273.15 30000.00 1418.96
273.15 40000.00 1461.31
273.15 50000.00 1499.98
273.15 60000.00 1535.77
273.15 70000.00 1570.58
273.15 80000.00 1604.15
273.15 90000.00 1636.02
273.15 100000.00 1666.45
278.15 100.00 1253.32
278.15 10000.00 1306.75
278.15 20000.00 1355.49
278.15 30000.00 1400.47
278.15 40000.00 1443.03
278.15 50000.00 1481.78
278.15 60000.00 1518.62
278.15 70000.00 1553.98
278.15 80000.00 1587.94
278.15 90000.00 1620.26
278.15 100000.00 1650.92
283.15 100.00 1231.06
283.15 10000.00 1285.85
283.15 20000.00 1335.74
283.15 30000.00 1381.4
283.15 40000.00 1424.94
283.15 50000.00 1464.43
283.15 60000.00 1502.23
283.15 70000.00 1537.63
283.15 80000.00 1571.96
283.15 90000.00 1604.68
283.15 100000.00 1635.63
288.15 100.00 1208.58
288.15 10000.00 1265.05
288.15 20000.00 1316.19
288.15 30000.00 1362.56
288.15 40000.00 1407.06
288.15 50000.00 1447.7
288.15 60000.00 1485.52
288.15 70000.00 1521.53
288.15 80000.00 1556.22
288.15 90000.00 1589.2
288.15 100000.00 1620.74
293.15 100.00 1186.09
293.15 10000.00 1244.14
293.15 20000.00 1296.86
293.15 30000.00 1344.06
293.15 40000.00 1389.16
293.15 50000.00 1430.7
293.15 60000.00 1469.0
293.15 70000.00 1505.7
293.15 80000.00 1540.77
293.15 90000.00 1574.27
293.15 100000.00 1605.01
298.15 100.00 1165.34
298.15 10000.00 1223.74
298.15 20000.00 1277.93
298.15 30000.00 1325.68
298.15 40000.00 1371.61
298.15 50000.00 1413.84
298.15 60000.00 1452.64
298.15 70000.00 1490.14
298.15 80000.00 1525.25
298.15 90000.00 1559.14
298.15 100000.00 1591.53
Reference

Correlations

Property Value Unit Temperature (K) Source
Cp,gas [55.25; 188.18] 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 A5.29150e+01
Coefficient B-6.69270e+02
Coefficient C5.29324e+00
Coefficient D1.28390e-04
Coefficient E-5.88440e-08
Temperature range, min.150.00
Temperature range, max.1500.00
Cp,gas 55.25 J/mol×K 150.00 Calculated Property
Cp,gas 75.01 J/mol×K 300.00 Calculated Property
Cp,gas 99.99 J/mol×K 450.00 Calculated Property
Cp,gas 121.88 J/mol×K 600.00 Calculated Property
Cp,gas 139.76 J/mol×K 750.00 Calculated Property
Cp,gas 154.16 J/mol×K 900.00 Calculated Property
Cp,gas 165.73 J/mol×K 1050.00 Calculated Property
Cp,gas 175.02 J/mol×K 1200.00 Calculated Property
Cp,gas 182.40 J/mol×K 1350.00 Calculated Property
Cp,gas 188.18 J/mol×K 1500.00 Calculated Property
Property Value Unit Temperature (K) Source
Cp,liquid [117.00; 132.79] J/mol×K [178.45; 329.44] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is Cp,liquid in J/mol×K, T in K
Coefficient A1.07130e+02
Coefficient B7.25570e+02
Coefficient C-5.95480e+00
Coefficient D2.59810e-02
Coefficient E-1.43900e-05
Temperature range, min.178.45
Temperature range, max.329.44
Cp,liquid 117.00 J/mol×K 178.45 Calculated Property
Cp,liquid 116.96 J/mol×K 195.23 Calculated Property
Cp,liquid 117.40 J/mol×K 212.00 Calculated Property
Cp,liquid 118.24 J/mol×K 228.78 Calculated Property
Cp,liquid 119.46 J/mol×K 245.56 Calculated Property
Cp,liquid 121.09 J/mol×K 262.33 Calculated Property
Cp,liquid 123.17 J/mol×K 279.11 Calculated Property
Cp,liquid 125.76 J/mol×K 295.89 Calculated Property
Cp,liquid 128.94 J/mol×K 312.66 Calculated Property
Cp,liquid 132.79 J/mol×K 329.44 Calculated Property
Property Value Unit Temperature (K) Source
η [0.0016558; 0.0001478] Pa×s [190.00; 408.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = exp(A + B/T + C·ln(T) + D·T^E)
Y is η in Pa×s, T in K
Coefficient A-1.40640e+01
Coefficient B1.00070e+03
Coefficient C4.53490e-01
Coefficient D3.94560e-07
Coefficient E2.00000e+00
Temperature range, min.190.00
Temperature range, max.408.00
η 0.0016558 Pa×s 190.00 Calculated Property
η 0.0009676 Pa×s 214.22 Calculated Property
η 0.0006347 Pa×s 238.44 Calculated Property
η 0.0004525 Pa×s 262.67 Calculated Property
η 0.0003432 Pa×s 286.89 Calculated Property
η 0.0002730 Pa×s 311.11 Calculated Property
η 0.0002252 Pa×s 335.33 Calculated Property
η 0.0001914 Pa×s 359.56 Calculated Property
η 0.0001666 Pa×s 383.78 Calculated Property
η 0.0001478 Pa×s 408.00 Calculated Property
Property Value Unit Temperature (K) Source
ΔvapH [36.55; 0.00] kJ/mol [178.45; 508.10] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc
Y is ΔvapH in kJ/mol, T in K
Coefficient A6.69430e+01
Coefficient B3.47360e+00
Coefficient C-8.92710e+00
Coefficient D1.00620e+01
Coefficient E-4.16560e+00
Critical temperature, Tc (K)5.08100e+02
CommentRange stopped at Tc; ChemSep gives it to 508.15 K.
Temperature range, min.178.45
Temperature range, max.508.10
ΔvapH 36.55 kJ/mol 178.45 Calculated Property
ΔvapH 34.93 kJ/mol 215.08 Calculated Property
ΔvapH 33.46 kJ/mol 251.71 Calculated Property
ΔvapH 31.84 kJ/mol 288.33 Calculated Property
ΔvapH 29.89 kJ/mol 324.96 Calculated Property
ΔvapH 27.51 kJ/mol 361.59 Calculated Property
ΔvapH 24.66 kJ/mol 398.22 Calculated Property
ΔvapH 21.26 kJ/mol 434.84 Calculated Property
ΔvapH 16.81 kJ/mol 471.47 Calculated Property
ΔvapH 0.00 kJ/mol 508.10 Calculated Property
Property Value Unit Temperature (K) Source
Pvap [1.33; 4731.33] kPa [240.93; 508.10] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.48340e+01
Coefficient B-3.02945e+03
Coefficient C-3.26710e+01
Temperature range, min.240.93
Temperature range, max.508.10
Pvap 1.33 kPa 240.93 Calculated Property
Pvap 8.18 kPa 270.62 Calculated Property
Pvap 33.60 kPa 300.30 Calculated Property
Pvap 104.03 kPa 329.99 Calculated Property
Pvap 262.34 kPa 359.67 Calculated Property
Pvap 567.19 kPa 389.36 Calculated Property
Pvap 1089.25 kPa 419.04 Calculated Property
Pvap 1905.84 kPa 448.73 Calculated Property
Pvap 3095.17 kPa 478.41 Calculated Property
Pvap 4731.33 kPa 508.10 Calculated Property
Pvap [2.56e-03; 4713.88] kPa [178.45; 508.10] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = exp(A + B/T + C·ln(T) + D·T^E)
Y is Pvap in kPa, T in K
Coefficient A6.58694e+01
Coefficient B-5.75294e+03
Coefficient C-7.68008e+00
Coefficient D6.83076e-06
Coefficient E2.00000e+00
CommentRange stopped at Tc; ChemSep gives it to 508.2 K.
Temperature range, min.178.45
Temperature range, max.508.10
Pvap 2.56e-03 kPa 178.45 Calculated Property
Pvap 0.16 kPa 215.08 Calculated Property
Pvap 2.69 kPa 251.71 Calculated Property
Pvap 19.77 kPa 288.33 Calculated Property
Pvap 87.17 kPa 324.96 Calculated Property
Pvap 273.89 kPa 361.59 Calculated Property
Pvap 682.11 kPa 398.22 Calculated Property
Pvap 1443.34 kPa 434.84 Calculated Property
Pvap 2719.42 kPa 471.47 Calculated Property
Pvap 4713.88 kPa 508.10 Calculated Property
Pvap [2.57e-03; 4695.88] kPa [178.45; 508.20] 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 A6.69693e+01
Coefficient B-5.78459e+03
Coefficient C-7.85881e+00
Coefficient D7.10496e-06
Coefficient E0.00000e+00
Temperature range, min.178.45
Temperature range, max.508.20
Pvap 2.57e-03 kPa 178.45 Calculated Property
Pvap 0.16 kPa 215.09 Calculated Property
Pvap 2.70 kPa 251.73 Calculated Property
Pvap 19.81 kPa 288.37 Calculated Property
Pvap 87.11 kPa 325.01 Calculated Property
Pvap 273.04 kPa 361.64 Calculated Property
Pvap 678.92 kPa 398.28 Calculated Property
Pvap 1435.57 kPa 434.92 Calculated Property
Pvap 2705.52 kPa 471.56 Calculated Property
Pvap 4695.88 kPa 508.20 Calculated Property
Pvap [4.33; 4599.85] kPa [259.16; 507.60] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.47929e+01
Coefficient B-3.02157e+03
Coefficient C-3.24450e+01
ReferenceAmbrose, Sprake, et al., 1974
CommentCoefficents calculated by NIST from author's data.
Temperature range, min.259.16
Temperature range, max.507.60
Pvap 4.33 kPa 259.16 Calculated Property
Pvap 18.39 kPa 286.76 Calculated Property
Pvap 58.86 kPa 314.37 Calculated Property
Pvap 153.09 kPa 341.97 Calculated Property
Pvap 340.48 kPa 369.58 Calculated Property
Pvap 670.93 kPa 397.18 Calculated Property
Pvap 1201.74 kPa 424.79 Calculated Property
Pvap 1993.73 kPa 452.39 Calculated Property
Pvap 3107.44 kPa 480.00 Calculated Property
Pvap 4599.85 kPa 507.60 Calculated Property
Property Value Unit Temperature (K) Source
ρl [910.19; 300.35] kg/m3 [178.00; 508.10] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A / B^(1 + (1 − T/C)^D)
Y is ρl in kg/m3, T in K
Coefficient A6.41833e+01
Coefficient B2.45560e-01
Coefficient C5.08210e+02
Coefficient D2.74090e-01
CommentRange stopped at Tc; ChemSep gives it to 508.2 K.
Temperature range, min.178.00
Temperature range, max.508.10
ρl 910.19 kg/m3 178.00 Calculated Property
ρl 874.83 kg/m3 214.68 Calculated Property
ρl 837.68 kg/m3 251.36 Calculated Property
ρl 798.29 kg/m3 288.03 Calculated Property
ρl 756.03 kg/m3 324.71 Calculated Property
ρl 709.88 kg/m3 361.39 Calculated Property
ρl 658.13 kg/m3 398.07 Calculated Property
ρl 597.28 kg/m3 434.74 Calculated Property
ρl 517.84 kg/m3 471.42 Calculated Property
ρl 300.35 kg/m3 508.10 Calculated Property
Property Value Unit Temperature (K) Source
γ [0.04; 0.02] N/m [179.15; 329.15] Jasper (1972), surface tension of pure liquid compounds Compiled value Show Hide
EquationY = A + B·T + C·T² + D·T³ + E·T⁴
Y is γ in N/m, T in K
Coefficient A5.68528e-02
Coefficient B-1.12000e-04
Coefficient C0.00000e+00
Coefficient D0.00000e+00
Coefficient E0.00000e+00
Temperature range, min.179.15
Temperature range, max.329.15
γ 0.04 N/m 179.15 Calculated Property
γ 0.03 N/m 195.82 Calculated Property
γ 0.03 N/m 212.48 Calculated Property
γ 0.03 N/m 229.15 Calculated Property
γ 0.03 N/m 245.82 Calculated Property
γ 0.03 N/m 262.48 Calculated Property
γ 0.03 N/m 279.15 Calculated Property
γ 0.02 N/m 295.82 Calculated Property
γ 0.02 N/m 312.48 Calculated Property
γ 0.02 N/m 329.15 Calculated Property
γ [0.04; 0.00] N/m [178.45; 490.84] 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-3.67690e-02
Coefficient B-1.48350e+00
Coefficient C-2.31500e+00
Coefficient D-1.24730e-03
Coefficient E-1.40400e-06
Temperature range, min.178.45
Temperature range, max.490.84
γ 0.04 N/m 178.45 Calculated Property
γ 0.03 N/m 213.16 Calculated Property
γ 0.03 N/m 247.87 Calculated Property
γ 0.02 N/m 282.58 Calculated Property
γ 0.02 N/m 317.29 Calculated Property
γ 0.02 N/m 352.00 Calculated Property
γ 0.01 N/m 386.71 Calculated Property
γ 0.01 N/m 421.42 Calculated Property
γ 0.00 N/m 456.13 Calculated Property
γ 0.00 N/m 490.84 Calculated Property
Property Value Unit Temperature (K) Source
λgas [0.00; 0.11] W/m×K [178.45; 1000.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A·T^B / (1 + C/T + D/T²)
Y is λgas in W/m×K, T in K
Coefficient A-2.68820e+01
Coefficient B9.03600e-01
Coefficient C-1.20950e+08
Coefficient D-6.08790e+08
Temperature range, min.178.45
Temperature range, max.1000.00
λgas 0.00 W/m×K 178.45 Calculated Property
λgas 0.01 W/m×K 269.73 Calculated Property
λgas 0.02 W/m×K 361.02 Calculated Property
λgas 0.02 W/m×K 452.30 Calculated Property
λgas 0.04 W/m×K 543.58 Calculated Property
λgas 0.05 W/m×K 634.87 Calculated Property
λgas 0.06 W/m×K 726.15 Calculated Property
λgas 0.08 W/m×K 817.43 Calculated Property
λgas 0.09 W/m×K 908.72 Calculated Property
λgas 0.11 W/m×K 1000.00 Calculated Property
Property Value Unit Temperature (K) Source
λliquid [0.21; 0.14] W/m×K [178.45; 343.15] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is λliquid in W/m×K, T in K
Coefficient A1.01300e-02
Coefficient B-9.53200e+01
Coefficient C-2.11510e-01
Coefficient D-5.26160e-03
Coefficient E2.30430e-06
Temperature range, min.178.45
Temperature range, max.343.15
λliquid 0.21 W/m×K 178.45 Calculated Property
λliquid 0.20 W/m×K 196.75 Calculated Property
λliquid 0.20 W/m×K 215.05 Calculated Property
λliquid 0.19 W/m×K 233.35 Calculated Property
λliquid 0.18 W/m×K 251.65 Calculated Property
λliquid 0.17 W/m×K 269.95 Calculated Property
λliquid 0.16 W/m×K 288.25 Calculated Property
λliquid 0.16 W/m×K 306.55 Calculated Property
λliquid 0.15 W/m×K 324.85 Calculated Property
λliquid 0.14 W/m×K 343.15 Calculated Property

Similar Compounds

CH2COCH3. Acetone-D6. Methyl glyoxal. C(CH3)2. Acetyl cyanide. 2-Propanone, 1-fluoro-. Bromoacetone. 2-Propanone, 1-chloro-. 3-Butyne-2-one. Isopropyl radical. 2-C3H7+. Neopentane. Neopentyl radical. NCC(CH3)CO. 2-Propanone, 1,1,1-trifluoro-.

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Mixtures

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