Chemical Properties of Acetic acid (CAS 64-19-7)

Acetic acid

InChI
InChI=1S/C2H4O2/c1-2(3)4/h1H3,(H,3,4)
InChI Key
QTBSBXVTEAMEQO-UHFFFAOYSA-N
Formula
C2H4O2
SMILES
CC(=O)O
Molecular Weight1
60.05
CAS
64-19-7
Other Names
  • Acetasol
  • Acetic acid, glacial
  • Aci-jel
  • Acide acetique
  • Acido acetico
  • Azijnzuur
  • CH3COOH
  • Essigsaeure
  • Ethanoic acid monomer
  • Ethylic acid
  • Glacial acetic acid
  • Kyselina octova
  • NSC 132953
  • Octowy kwas
  • Shotgun
  • UN 2789
  • Vinegar acid
  • ethanoic acid
  • methanecarboxylic acid
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Physical Properties

Property Value Unit Source
ω [0.4218; 0.4600]   Show Hide
ω 0.4218 PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω 0.4600 ChemSep v8.3 pure component data Compiled value
ω 0.4470 KDB
PAff 783.70 kJ/mol NIST
Tig [699.82; 736.15] K Show Hide
Tig 699.82 K KDB
Tig 736.15 K NCMS SOLV-DB
BasG 752.80 kJ/mol NIST
ΔcH°liquid [-875.16; -872.40] kJ/mol Show Hide
ΔcH°liquid -875.16 ± 0.34 kJ/mol NIST
ΔcH°liquid -874.20 ± 0.20 kJ/mol NIST
ΔcH°liquid -874.50 ± 0.40 kJ/mol NIST
ΔcH°liquid -872.40 kJ/mol NIST
μ [1.30; 1.74] debye Show Hide
μ 1.74 debye ChemSep v8.3 pure component data Compiled value
μ 1.30 debye KDB
εr 6.17 NCMS SOLV-DB
LFL 5.40 % in Air KDB
UFL 16.00 % in Air KDB
Tflash,cc [312.15; 317.59] K Show Hide
Tflash,cc 317.59 K KDB
Tflash,cc 312.15 K NCMS SOLV-DB
Tflash,oc 313.15 K KDB
ΔfG° [-376.90; -374.50] kJ/mol Show Hide
ΔfG° -374.50 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfG° -376.90 kJ/mol KDB
Rg 2.5950 KDB
ΔfH°gas [-435.40; -431.90] kJ/mol Show Hide
ΔfH°gas -432.80 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfH°gas -435.10 kJ/mol KDB
ΔfH°gas -431.90 ± 1.50 kJ/mol NIST
ΔfH°gas -431.90 ± 1.50 kJ/mol NIST
ΔfH°gas -432.90 ± 1.50 kJ/mol NIST
ΔfH°gas -432.90 ± 1.50 kJ/mol NIST
ΔfH°gas -432.50 ± 1.60 kJ/mol NIST
ΔfH°gas -432.50 ± 1.60 kJ/mol NIST
ΔfH°gas -435.40 kJ/mol NIST
ΔfH°gas -435.40 ± 4.30 kJ/mol NIST
ΔfH°liquid [-487.00; -483.52] kJ/mol Show Hide
ΔfH°liquid -483.52 ± 0.36 kJ/mol NIST
ΔfH°liquid -484.50 ± 0.20 kJ/mol NIST
ΔfH°liquid -484.10 ± 0.40 kJ/mol NIST
ΔfH°liquid -487.00 kJ/mol NIST
ΔfusH° 11.08 kJ/mol Joback Calculated Property
ΔvapH° [23.35; 51.60] kJ/mol Show Hide
ΔvapH° 23.35 kJ/mol NCMS SOLV-DB
ΔvapH° 50.30 kJ/mol NIST
ΔvapH° 51.60 kJ/mol NIST
ΔvapH° 51.60 ± 1.50 kJ/mol NIST
ΔvapH° 51.60 ± 1.60 kJ/mol NIST
IE [10.35; 11.50] eV Show Hide
IE 10.65 ± 0.02 eV NIST
IE 10.63 eV NIST
IE 10.66 eV NIST
IE 10.66 ± 0.05 eV NIST
IE 10.66 eV NIST
IE 10.66 ± 0.05 eV NIST
IE 10.66 ± 0.00 eV NIST
IE 10.64 ± 0.00 eV NIST
IE 10.65 eV NIST
IE 10.69 ± 0.03 eV NIST
IE 10.70 eV NIST
IE 10.37 ± 0.03 eV NIST
IE 10.38 ± 0.03 eV NIST
IE 10.35 ± 0.03 eV NIST
IE 10.90 eV NIST
IE 10.84 eV NIST
IE 10.63 eV NIST
IE Outlier 11.50 eV NIST
IE 10.87 eV NIST
IE 10.80 eV NIST
log10WS 1.22 Aq. Solubility Prediction
logPoct/wat -0.170 NCMS SOLV-DB
McVol 46.480 ml/mol McGowan Calculated Property
NFPA Fire [%!d(float64=2); %!d(float64=2)]   Show Hide
NFPA Fire 2 KDB
NFPA Fire 2 NCMS SOLV-DB
NFPA Health [%!d(float64=2); %!d(float64=3)]   Show Hide
NFPA Health 3 KDB
NFPA Health 2 NCMS SOLV-DB
NFPA Safety [%!d(float64=1); %!d(float64=1)]   Show Hide
NFPA Safety 1 KDB
NFPA Safety 1 NCMS SOLV-DB
Pc [5780.00; 5829.01] kPa Show Hide
Pc 5780.00 kPa IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Pc 5785.66 kPa PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc 5790.00 kPa ChemSep v8.3 pure component data Compiled value
Pc 5786.00 kPa KDB
Pc 5781.00 ± 20.00 kPa NIST
Pc Outlier 5829.01 ± 90.00 kPa NIST
Pc 5786.00 ± 8.00 kPa NIST
Pc 5787.00 ± 101.32 kPa NIST
Pc 5786.70 ± 26.66 kPa NIST
pKa 4.76 NCMS SOLV-DB
Ptriple [1.28; 1.28] kPa Show Hide
Ptriple 1.28 kPa ChemSep v8.3 pure component data Compiled value
Ptriple 1.28 kPa KDB
ρc [350.58; 350.70] kg/m3 Show Hide
ρc 350.70 ± 1.20 kg/m3 NIST
ρc 350.58 ± 1.20 kg/m3 NIST
Inp [580.00; 665.00]   Show Hide
Inp 590.00 NIST
Inp 602.00 NIST
Inp 646.00 NIST
Inp 645.00 NIST
Inp 602.00 NIST
Inp 661.00 NIST
Inp 600.00 NIST
Inp 600.00 NIST
Inp 625.00 NIST
Inp 649.00 NIST
Inp 600.00 NIST
Inp 663.00 NIST
Inp 606.00 NIST
Inp 660.40 NIST
Inp 625.00 NIST
Inp 625.00 NIST
Inp 600.00 NIST
Inp 599.00 NIST
Inp 594.00 NIST
Inp 600.00 NIST
Inp 605.00 NIST
Inp 610.00 NIST
Inp Outlier 665.00 NIST
Inp 600.00 NIST
Inp 610.00 NIST
Inp 610.00 NIST
Inp 645.00 NIST
Inp 642.00 NIST
Inp 642.00 NIST
Inp 609.00 NIST
Inp 640.00 NIST
Inp 587.00 NIST
Inp 588.00 NIST
Inp 623.00 NIST
Inp 602.00 NIST
Inp 641.00 NIST
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Inp 610.00 NIST
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Inp 615.00 NIST
Inp 615.00 NIST
Inp 662.00 NIST
Inp 658.00 NIST
Inp 600.00 NIST
Inp 660.00 NIST
Inp 649.00 NIST
Inp 638.00 NIST
Inp 660.00 NIST
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Inp 600.00 NIST
Inp 617.00 NIST
Inp 617.00 NIST
Inp 603.00 NIST
Inp 603.00 NIST
Inp 606.00 NIST
Inp 584.00 NIST
Inp 637.00 NIST
Inp 628.00 NIST
Inp 628.00 NIST
Inp 580.00 NIST
Inp 620.77 NIST
Inp 616.00 NIST
Inp 650.00 NIST
Inp 650.00 NIST
Inp 608.00 NIST
Inp 602.00 NIST
Inp 611.00 NIST
Inp 600.00 NIST
Inp 622.00 NIST
Inp 646.00 NIST
Inp 621.00 NIST
Inp 630.00 NIST
Inp 662.00 NIST
Inp 600.00 NIST
Inp 600.00 NIST
Inp 600.00 NIST
Inp 600.00 NIST
Inp 606.00 NIST
Inp 595.00 NIST
Inp 638.00 NIST
Inp 610.00 NIST
Inp 600.00 NIST
Inp 600.00 NIST
Inp 594.00 NIST
Inp 601.00 NIST
Inp 616.00 NIST
Inp 618.00 NIST
Inp 622.00 NIST
Inp 606.00 NIST
Inp 610.00 NIST
Inp 610.00 NIST
Inp 610.00 NIST
Inp 610.00 NIST
Inp 610.00 NIST
Inp 591.00 NIST
Inp 591.00 NIST
Inp 630.00 NIST
Inp 612.00 NIST
Inp 644.00 NIST
Inp 612.00 NIST
Inp 614.00 NIST
Inp 622.00 NIST
Inp 645.00 NIST
Inp 600.00 NIST
Inp 645.00 NIST
Inp 645.00 NIST
Inp 634.00 NIST
Inp 648.00 NIST
Inp 648.00 NIST
Inp 660.00 NIST
Inp 660.00 NIST
Inp 600.00 NIST
Inp 610.00 NIST
Inp 645.00 NIST
Inp 590.00 NIST
Inp 630.00 NIST
Inp 618.00 NIST
Inp 622.00 NIST
Inp 634.00 NIST
Inp 602.00 NIST
Inp 663.00 NIST
Inp 609.00 NIST
Inp 615.00 NIST
Inp 660.00 NIST
Inp 606.00 NIST
Inp 580.00 NIST
Inp 608.00 NIST
Inp 646.00 NIST
Ip [1400.00; 1498.00]   Show Hide
Ip 1465.00 NIST
Ip 1465.00 NIST
Ip 1408.00 NIST
Ip Outlier 1400.00 NIST
Ip Outlier 1400.00 NIST
Ip 1447.00 NIST
Ip 1449.00 NIST
Ip 1452.00 NIST
Ip 1445.00 NIST
Ip 1435.00 NIST
Ip Outlier 1402.00 NIST
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Ip 1427.00 NIST
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Ip 1444.00 NIST
Ip 1418.00 NIST
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Ip 1433.00 NIST
Ip 1442.00 NIST
Ip 1449.00 NIST
Ip Outlier 1488.00 NIST
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Ip Outlier 1498.00 NIST
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Ip Outlier 1404.00 NIST
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Ip Outlier 1403.00 NIST
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Ip Outlier 1488.00 NIST
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Ip Outlier 1405.00 NIST
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Ip Outlier 1403.00 NIST
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Ip Outlier 1492.00 NIST
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Ip 1448.00 NIST
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Ip Outlier 1498.00 NIST
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Ip Outlier 1403.00 NIST
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S°gas 282.84 J/mol×K NIST
S°liquid [158.00; 193.70] J/mol×K Show Hide
S°liquid 158.00 J/mol×K NIST
S°liquid 193.70 J/mol×K NIST
Tboil [374.20; 392.40] K Show Hide
Tboil 391.20 K Liquid liquid equilibria of the ternary system water + acetic acid + dimethyl adipate
Tboil 390.95 K Vapor liquid equilibria for the quaternary reactive system ethyl acetate + ethanol +water + acetic acid and some of the constituent binary systems at 101.3 kPa
Tboil 391.20 K Liquid liquid equilibria of the ternary system water + acetic acid + dimethyl succinate
Tboil 390.85 K Isobaric vapor liquid equilibria for water + acetic acid + (N-methyl pyrrolidone or N-methyl acetamide)
Tboil 391.05 K Determination and correlation of liquid liquid equilibria for the (water + carboxylic acid + dimethyl maleate) ternary systems at T = 298.2K
Tboil 391.00 K Vapor liquid equilibria for water + acetic acid + (N,N-dimethylformamide or dimethyl sulfoxide) at 13.33 kPa
Tboil 391.05 K Quaternary phase equilibrium of water-carboxylic acid mixture (formic-propionic acid or acetic-propionic acid)-solvent liquid systems at 298.15 K
Tboil 390.95 K Ternary liquid-liquid phase equilibria of (water-carboxylic acid-1-undecanol) systems at 298.15 K
Tboil 391.03 K Isobaric vapor-liquid equilibrium for water + acetic acid + 1-butyl-3-methylimidazolium dibutylphosphate at 101.32 kPa
Tboil 391.20 K (Liquid + liquid) equilibria of the (water + acetic acid + dibutyl phthalate) system
Tboil 390.93 K Study of Vapor-Liquid Equilibria for Acetic Acid + n-Propyl Acetate + Isopropyl Acetate Systems
Tboil 391.20 K Liquid-Liquid Equilibria of Water + Acetic Acid + Dimethyl Glutarate Ternary System
Tboil 390.85 K Measurements of Quaternary Liquid-Liquid Equilibrium for Water + Acetic Acid + Propionic Acid + Solvent (Butyronitrile, Benzyl Acetate, or Methyl Isobutyl Ketone) at 298.15 K
Tboil 391.03 K Isobaric Vapor-Liquid Equilibria for Water + Acetic Acid + 1- Ethyl-3-methylimidazolium Diethylphosphate at 101.32 kPa
Tboil 390.96 K Investigation on Isobaric Vapor Liquid Equilibrium for Water + Acetic Acid + sec-Butyl Acetate
Tboil 391.15 K Liquid-Liquid Equilibria of (Water + Acetic Acid + Diethyl Succinate or Diethyl Glutarate or Diethyl Adipate) Ternary Systems
Tboil 391.44 K Isobaric Vapor-Liquid Equilibria for (Acetic Acid + Cyclohexane) and (Cyclohexane + Acetylacetone) at a Pressure of 101.3 kPa and for (Acetic Acid + Acetylacetone) at a Pressure of 60.0 kPa
Tboil 391.04 K ChemSep v8.3 pure component data Compiled value
Tboil 391.00 K KDB
Tboil 391.03 K NCMS SOLV-DB
Tboil 391.05 ± 0.20 K NIST
Tboil 391.20 ± 0.20 K NIST
Tboil 391.09 ± 0.30 K NIST
Tboil 391.10 ± 0.15 K NIST
Tboil 391.10 K NIST
Tboil 391.30 ± 0.50 K NIST
Tboil 390.20 ± 0.50 K NIST
Tboil 392.00 ± 2.00 K NIST
Tboil 391.30 ± 0.50 K NIST
Tboil 390.78 ± 0.30 K NIST
Tboil 391.70 ± 0.30 K NIST
Tboil 391.10 K NIST
Tboil 391.30 ± 0.50 K NIST
Tboil 391.40 ± 0.30 K NIST
Tboil 391.30 ± 0.30 K NIST
Tboil 391.10 ± 0.30 K NIST
Tboil 391.30 ± 0.30 K NIST
Tboil 391.05 ± 0.15 K NIST
Tboil 391.30 ± 0.40 K NIST
Tboil 391.10 ± 0.20 K NIST
Tboil 391.10 ± 0.15 K NIST
Tboil 391.36 ± 0.15 K NIST
Tboil 391.40 ± 0.20 K NIST
Tboil 391.30 ± 0.30 K NIST
Tboil 390.50 ± 1.00 K NIST
Tboil 391.10 ± 0.40 K NIST
Tboil 391.20 ± 0.20 K NIST
Tboil 391.00 ± 1.00 K NIST
Tboil 390.70 ± 1.00 K NIST
Tboil 391.41 ± 0.40 K NIST
Tboil 391.90 ± 0.20 K NIST
Tboil 391.30 ± 0.50 K NIST
Tboil 391.30 ± 0.50 K NIST
Tboil 391.70 ± 0.50 K NIST
Tboil 389.00 ± 2.00 K NIST
Tboil 391.70 ± 0.50 K NIST
Tboil 391.30 ± 0.50 K NIST
Tboil 389.80 ± 2.00 K NIST
Tboil 390.85 ± 0.50 K NIST
Tboil 391.00 ± 0.15 K NIST
Tboil 391.10 ± 0.15 K NIST
Tboil 391.07 ± 0.15 K NIST
Tboil 391.10 ± 0.15 K NIST
Tboil 391.30 ± 0.50 K NIST
Tboil 389.70 ± 2.00 K NIST
Tboil 390.87 ± 0.30 K NIST
Tboil 391.30 ± 0.50 K NIST
Tboil 391.00 ± 1.00 K NIST
Tboil 391.00 ± 1.00 K NIST
Tboil 391.20 ± 0.30 K NIST
Tboil 391.00 ± 1.00 K NIST
Tboil 391.30 ± 0.50 K NIST
Tboil 391.30 ± 0.40 K NIST
Tboil 391.70 ± 1.00 K NIST
Tboil 391.40 ± 0.50 K NIST
Tboil 391.30 ± 0.20 K NIST
Tboil 391.30 ± 0.50 K NIST
Tboil Outlier 386.00 ± 5.00 K NIST
Tboil 391.00 ± 0.50 K NIST
Tboil 391.00 ± 0.20 K NIST
Tboil 391.50 ± 0.40 K NIST
Tboil 391.00 ± 0.50 K NIST
Tboil 391.00 ± 0.40 K NIST
Tboil 391.40 ± 0.30 K NIST
Tboil 391.00 ± 0.40 K NIST
Tboil 392.40 ± 1.00 K NIST
Tboil 391.00 ± 1.00 K NIST
Tboil 391.00 ± 0.40 K NIST
Tboil 391.00 ± 0.40 K NIST
Tboil 391.30 ± 0.50 K NIST
Tboil 391.50 ± 0.50 K NIST
Tboil 390.90 ± 1.00 K NIST
Tboil 391.00 ± 1.00 K NIST
Tboil Outlier 374.20 ± 0.40 K NIST
Tboil 391.90 ± 0.60 K NIST
Tboil 391.26 ± 0.30 K NIST
Tboil 388.70 ± 5.00 K NIST
Tboil 391.00 ± 1.00 K NIST
Tboil 391.70 ± 0.40 K NIST
Tboil Outlier 382.70 ± 10.00 K NIST
Tboil 391.00 ± 1.00 K NIST
Tboil 389.70 ± 2.00 K NIST
Tboil 391.20 ± 0.60 K NIST
Tboil 391.40 ± 0.40 K NIST
Tboil 391.60 ± 0.40 K NIST
Tboil 391.30 ± 0.50 K NIST
Tboil 390.30 ± 1.00 K NIST
Tboil 391.30 ± 0.60 K NIST
Tboil 391.25 ± 0.60 K NIST
Tboil 390.45 ± 1.50 K NIST
Tboil 390.45 ± 1.50 K NIST
Tc [590.70; 594.80] K Show Hide
Tc 590.70 K IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Tc 594.40 K PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc 594.45 K ChemSep v8.3 pure component data Compiled value
Tc 592.71 K KDB
Tc 592.90 ± 1.00 K NIST
Tc 590.70 ± 0.40 K NIST
Tc 590.84 ± 2.00 K NIST
Tc 592.70 K NIST
Tc 592.71 ± 0.07 K NIST
Tc 594.35 ± 0.40 K NIST
Tc 594.45 ± 0.40 K NIST
Tc 594.50 ± 0.40 K NIST
Tc 594.75 ± 4.00 K NIST
Tc 594.80 ± 4.00 K NIST
Tfus [289.00; 289.95] K Show Hide
Tfus 289.84 K Solid liquid equilibrium in the ternary system acetic acid propanoic acid formamide
Tfus 289.95 K Differential scanning calorimetry determination of phase diagrams and water activities of aqueous carboxylic acid solutions
Tfus 289.85 K Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus 289.81 K ChemSep v8.3 pure component data Compiled value
Tfus 289.70 K KDB
Tfus 289.93 K Aq. Solubility Prediction
Tfus 289.81 K NCMS SOLV-DB
Tfus 289.70 ± 0.03 K NIST
Tfus 289.85 K NIST
Tfus 289.62 ± 0.10 K NIST
Tfus 289.49 ± 0.05 K NIST
Tfus 289.75 ± 0.05 K NIST
Tfus 289.80 ± 0.30 K NIST
Tfus 289.67 ± 0.05 K NIST
Tfus Outlier 289.00 ± 1.50 K NIST
Tfus 289.69 ± 0.20 K NIST
Ttriple [289.69; 289.81] K Show Hide
Ttriple 289.81 K ChemSep v8.3 pure component data Compiled value
Ttriple 289.69 K KDB
Ttriple 289.80 ± 0.05 K NIST
Ttriple 289.69 ± 0.04 K NIST
Ttriple 289.80 ± 0.15 K NIST
Ttriple 289.69 ± 0.04 K NIST
Ttriple 289.80 ± 0.15 K NIST
UQi 2.04 ChemSep v8.3 pure component data Compiled value
URi 2.23 ChemSep v8.3 pure component data Compiled value
Vc [0.171; 0.171] m3/kmol Show Hide
Vc 0.171 m3/kmol IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Vc 0.171 m3/kmol PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc 0.171 m3/kmol ChemSep v8.3 pure component data Compiled value
Vc 0.171 m3/kmol KDB
Zc [0.2000000; 0.2010000]   Show Hide
Zc 0.2010000 IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Zc 0.2000000 ChemSep v8.3 pure component data Compiled value
Zc 0.2007690 KDB
Zra 0.22 KDB

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,liquid [120.50; 159.80] J/mol×K [294.70; 333.15] Show Hide
Cp,liquid 123.40 J/mol×K 294.70 NIST
Cp,liquid 121.30 J/mol×K 297.10 NIST
Cp,liquid 120.50 J/mol×K 298.00 NIST
Cp,liquid 123.50 J/mol×K 298.00 NIST
Cp,liquid 159.80 J/mol×K 298.10 NIST
Cp,liquid 123.10 J/mol×K 298.15 NIST
Cp,liquid 137.00 J/mol×K 311.00 NIST
Cp,liquid 135.50 J/mol×K 313.15 Heat Capacities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
Cp,liquid 139.70 J/mol×K 332.00 NIST
Cp,liquid 137.21 J/mol×K 333.15 Heat Capacities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
η [0.0005700; 0.0012110] Pa×s [293.15; 353.15] Show Hide
η 0.0012040 Pa×s 293.15 Densities and Viscosities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
η 0.0012110 Pa×s 293.15 Dynamic Viscosities, Densities, and Speed of Sound and Derived Properties of the Binary Systems Acetic Acid with Water, Methanol, Ethanol, Ethyl Acetate and Methyl Acetate at T = (293.15, 298.15, and 303.15) K at Atmospheric Pressure
η 0.0012040 Pa×s 293.15 Densities and Viscosities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
η 0.0011150 Pa×s 298.15 Dynamic Viscosities, Densities, and Speed of Sound and Derived Properties of the Binary Systems Acetic Acid with Water, Methanol, Ethanol, Ethyl Acetate and Methyl Acetate at T = (293.15, 298.15, and 303.15) K at Atmospheric Pressure
η 0.0011300 Pa×s 298.15 NCMS SOLV-DB
η 0.0011140 Pa×s 298.15 Densities and Viscosities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
η 0.0011140 Pa×s 298.15 Densities and Viscosities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
η 0.0010340 Pa×s 303.15 Dynamic Viscosities, Densities, and Speed of Sound and Derived Properties of the Binary Systems Acetic Acid with Water, Methanol, Ethanol, Ethyl Acetate and Methyl Acetate at T = (293.15, 298.15, and 303.15) K at Atmospheric Pressure
η 0.0010590 Pa×s 303.15 Densities and Viscosities of N,N-Dimethylformamide + Formic Acid, and + Acetic Acid in the Temperature Range from (303.15 to 353.15) K
η 0.0010370 Pa×s 303.15 Densities and Viscosities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
η 0.0010370 Pa×s 303.15 Densities and Viscosities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
η 0.0009640 Pa×s 308.15 Densities and Viscosities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
η 0.0009640 Pa×s 308.15 Densities and Viscosities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
η 0.0009200 Pa×s 313.15 Densities and Viscosities of N,N-Dimethylformamide + Formic Acid, and + Acetic Acid in the Temperature Range from (303.15 to 353.15) K
η 0.0009020 Pa×s 313.15 Densities and Viscosities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
η 0.0009020 Pa×s 313.15 Densities and Viscosities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
η 0.0008410 Pa×s 318.15 Densities and Viscosities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
η 0.0008410 Pa×s 318.15 Densities and Viscosities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
η 0.0007870 Pa×s 323.15 Densities and Viscosities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
η 0.0007870 Pa×s 323.15 Densities and Viscosities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
η 0.0008040 Pa×s 323.15 Densities and Viscosities of N,N-Dimethylformamide + Formic Acid, and + Acetic Acid in the Temperature Range from (303.15 to 353.15) K
η 0.0007410 Pa×s 328.15 Densities and Viscosities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
η 0.0007410 Pa×s 328.15 Densities and Viscosities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
η 0.0007090 Pa×s 333.15 Densities and Viscosities of N,N-Dimethylformamide + Formic Acid, and + Acetic Acid in the Temperature Range from (303.15 to 353.15) K
η 0.0006970 Pa×s 333.15 Densities and Viscosities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
η 0.0006970 Pa×s 333.15 Densities and Viscosities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
η 0.0006570 Pa×s 338.15 Densities and Viscosities of Binary Mixtures of Acetic Acid with Acetic Anhydride and Methenamine at Different Temperatures
η 0.0006320 Pa×s 343.15 Densities and Viscosities of N,N-Dimethylformamide + Formic Acid, and + Acetic Acid in the Temperature Range from (303.15 to 353.15) K
η 0.0005700 Pa×s 353.15 Densities and Viscosities of N,N-Dimethylformamide + Formic Acid, and + Acetic Acid in the Temperature Range from (303.15 to 353.15) K
ΔfusH [10.83; 11.73] kJ/mol [283.70; 298.70] Show Hide
ΔfusH 11.52 kJ/mol 283.70 NIST
ΔfusH 10.83 kJ/mol 289.80 NIST
ΔfusH 11.73 kJ/mol 289.90 NIST
ΔfusH 11.73 kJ/mol 289.90 NIST
ΔfusH 11.13 kJ/mol 290.06 NIST
ΔfusH 11.72 kJ/mol 298.70 NIST
ΔfusH 11.72 kJ/mol 298.70 NIST
ΔfusH 11.72 kJ/mol 298.70 NIST
ΔsubH [67.00; 70.00] kJ/mol [221.50; 221.50] Show Hide
ΔsubH 67.00 ± 1.00 kJ/mol 221.50 NIST
ΔsubH 70.00 ± 1.00 kJ/mol 221.50 NIST
ΔvapH [23.68; 43.00] kJ/mol [308.00; 559.00] Show Hide
ΔvapH 43.00 kJ/mol 308.00 NIST
ΔvapH 41.60 kJ/mol 340.50 NIST
ΔvapH 42.00 kJ/mol 343.00 NIST
ΔvapH 41.60 kJ/mol 351.00 NIST
ΔvapH 40.90 kJ/mol 357.50 NIST
ΔvapH 40.30 kJ/mol 358.00 NIST
ΔvapH 39.10 kJ/mol 364.00 NIST
ΔvapH 23.70 kJ/mol 391.10 NIST
ΔvapH 23.68 kJ/mol 391.30 KDB
ΔvapH 38.70 kJ/mol 419.00 NIST
ΔvapH 37.90 kJ/mol 470.50 NIST
ΔvapH 38.10 kJ/mol 486.00 NIST
ΔvapH 38.80 kJ/mol 559.00 NIST
Pvap [2.09; 101.32] kPa [298.15; 391.03] Show Hide
Pvap 2.09 kPa 298.15 NCMS SOLV-DB
Pvap 7.72 kPa 323.15 Isothermal vapour liquid equilibrium with chemical reaction in the quaternary water + methanol + acetic acid + methyl acetate system, and in five binary subsystems
Pvap 7.57 kPa 323.15 Vapor-Liquid Equilibria in the Propyl Acetate + Ethanoic Acid Binary System from (323.15 to 353.15) K: Measurement with a Static Method and Modeling with the NRTL, Wilson, UNIQUAC, and COSMO-SAC Approaches
Pvap 12.04 kPa 333.15 Vapor-Liquid Equilibria in the Propyl Acetate + Ethanoic Acid Binary System from (323.15 to 353.15) K: Measurement with a Static Method and Modeling with the NRTL, Wilson, UNIQUAC, and COSMO-SAC Approaches
Pvap 18.66 kPa 343.15 Vapor-Liquid Equilibria in the Propyl Acetate + Ethanoic Acid Binary System from (323.15 to 353.15) K: Measurement with a Static Method and Modeling with the NRTL, Wilson, UNIQUAC, and COSMO-SAC Approaches
Pvap 20.00 kPa 345.27 Isobaric Vapor Liquid Equilibrium for Binary Systems of Toluene + Acrylic Acid, Toluene + Acetic Acid, and Cyclohexane + Acrylic Acid at 20 kPa
Pvap 28.20 kPa 353.15 Vapor-Liquid Equilibria in the Propyl Acetate + Ethanoic Acid Binary System from (323.15 to 353.15) K: Measurement with a Static Method and Modeling with the NRTL, Wilson, UNIQUAC, and COSMO-SAC Approaches
Pvap 49.34 kPa 368.10 Separation of Furfural from Ternary Mixtures
Pvap 88.98 kPa 386.07 Separation of Furfural from Ternary Mixtures
Pvap 96.15 kPa 388.91 Vapor Liquid Equilibrium Data for Binary Mixtures of Acetic Acid + Anisole, Acetone + Anisole, and Isopropanol + Anisole at Pressure 96.15 kPa
Pvap 101.32 kPa 391.03 Isobaric Vapor-Liquid Equilibria for Water + Acetic Acid + 1- Ethyl-3-methylimidazolium Diethylphosphate at 101.32 kPa
n0 [1.36809; 1.37224]   [293.00; 303.15] Show Hide
n0 1.37200 293.00 Quaternary Liquid-Liquid Equilibrium of Water + Acetic Acid + Propionic Acid + Solvent (Amyl Alcohol, Cyclohexyl Acetate, or Toluene) Systems
n0 1.37200 293.15 Isobaric Vapor-Liquid Equilibria for the Binary Systems of Acetic Acid + Isopropenyl Acetate, Acetic Acid + Acetylacetone, and Water + Acetylacetone
n0 1.36870 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 1.37160 293.15 Solubilities of Phosphorus-Containing Compounds in Selected Solvents
n0 1.37130 293.15 Isobaric (vapour + liquid) equilibria data for the binary systems {1,2-dichloroethane (1) + toluene (2)} and {1,2-dichloroethane (1) + acetic acid (2)} at atmospheric pressure
n0 1.37224 293.15 Solubility, Thermodynamic Properties, and Derived Excess Properties of Benzoic Acid in (Acetic Acid + Water) and (Acetic Acid + Toluene) Binary Mixtures
n0 1.37180 293.15 Solubilities of Some Phosphaspirocyclic Compounds in Selected Solvents
n0 1.37210 293.15 Liquid liquid equilibria of ternary systems (water + carboxylic acid + cumene) at 298.15K
n0 1.37170 293.15 Measurement and Modeling of Liquid Liquid Equilibrium for the Systems Vinyl Acetate + Acetic Acid/Ethanol + Water at 298.15 and 308.15 K
n0 1.37190 293.15 Isobaric Vapor-Liquid Equilibria for Water + Acetic Acid + (n-Pentyl Acetate or Isopropyl Acetate)
n0 1.37203 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 1.36969 298.15 Refractive Index, Surface Tension, and Density of Aqueous Mixtures of Carboxylic Acids at 298.15 K
n0 1.37012 298.15 Solubility, Thermodynamic Properties, and Derived Excess Properties of Benzoic Acid in (Acetic Acid + Water) and (Acetic Acid + Toluene) Binary Mixtures
n0 1.37160 298.15 Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures of Methanol, Ethanoic Acid, and Propanoic Acid
n0 1.36980 298.15 Densities, Excess Molar Volumes, Viscosity, and Refractive Indices of Binary Mixtures of Ethanoic Acid and Trichloroethylene with Dimethylbenzenes at Different Temperatures
n0 1.37160 298.15 Geometric Structures of Associating Component Optimized toward Correlation and Prediction of Isobaric Vapor Liquid Equilibria for Binary and Ternary Mixtures of Ethanal, Ethanol, and Ethanoic Acid
n0 1.37000 298.15 Solubilities of Benzoic Acid and Phthalic Acid in Acetic Acid + Water Solvent Mixtures
n0 1.36960 298.15 Phase Equilibrium for the Esterification Reaction of Acetic Acid + Butan-1-ol at 101.3 kPa
n0 1.36960 298.15 Study of liquid liquid equilibrium of the systems isobutyl acetate + acetic acid +water and isobutyl alcohol + acetic acid +water at different temperatures
n0 1.36960 298.15 Liquid-Liquid Equilibria for the System 1-Methyl Propyl Ethanoate (1) + Acetic Acid (2) + Water (3) at (283.15 and 323.15) K
n0 1.36900 298.15 NCMS SOLV-DB
n0 1.36809 303.15 Solubility, Thermodynamic Properties, and Derived Excess Properties of Benzoic Acid in (Acetic Acid + Water) and (Acetic Acid + Toluene) Binary Mixtures
n0 1.37160 303.15 Phase equilibria measurements of ternary mixtures (sulfolane + a carboxylic acid + pentane) at 303.15 K
n0 1.37160 303.15 Liquid liquid equilibria measurements of ternary systems (acetonitrile + a carboxylic acid + dodecane) at 303.15 K
ρl [993.00; 1055.01] kg/m3 [288.15; 343.15] Show Hide
ρl 1053.00 kg/m3 288.15 Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl 1055.01 kg/m3 288.20 The impact of uni-univalent electrolytes on (water + acetic acid + toluene) equilibria: Representation with electrolyte-NRTL model
ρl 1049.00 kg/m3 293.00 KDB
ρl 1055.00 kg/m3 293.15 Measurement and modelling of static dielectric constants of aqueous solutions of methanol, ethanol and acetic acid at T = 293.15 K and 91.3 kPa
ρl 1052.50 kg/m3 293.15 Probe of Interactions of Acetic and Propionic Acids with 2',3'-N-Epoxypropyl-N-methyl-2-oxopyrrolidinium Salicylate Ionic Liquid
ρl 1048.93 kg/m3 293.15 Liquid-Liquid Phase Equilibria for Quinary, Quaternary, and Ternary Systems {Water + Furfural + Acetic Acid + Cyclopentyl Methyl Ether + CaCl2}: Measurement, Effect of Salt ,and Comparative Study
ρl 1052.00 kg/m3 293.15 Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl 1044.30 kg/m3 293.15 Phase equilibrium of (water + formic or acetic acid + ethyl heptanoate) ternary liquid systems at different temperatures
ρl 1049.80 kg/m3 293.20 Liquid-liquid equilibrium data and thermophysical properties for ternary systems composed of water, acetic acid and different solvents
ρl 1049.80 kg/m3 293.20 Liquid-liquid equilibrium data for ternary systems of water + acetic acid + acetate esters at 293.2 K and 303.2 K and ~ 95 kPa
ρl 1046.90 kg/m3 298.15 Probe of Interactions of Acetic and Propionic Acids with 2',3'-N-Epoxypropyl-N-methyl-2-oxopyrrolidinium Salicylate Ionic Liquid
ρl 1049.42 kg/m3 298.15 Liquid-liquid equilibria of water + acetic acid + 2-ethyl hexyl acetate ternary system
ρl 1044.12 kg/m3 298.15 Liquid Phase Equilibria of Aqueous Mixtures of Carboxylic Acids (C1-C4) with Ethylbenzene: Thermodynamic and Mathematical Modeling
ρl 1043.50 kg/m3 298.15 Isobaric vapor-liquid equilibrium of the binary system sec-butyl acetate + para-xylene and the quaternary system methyl acetate + para-xylene + sec-butyl acetate + acetic acid at 101.3 kPa
ρl 1044.60 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 1042.00 kg/m3 298.15 Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl 1043.67 kg/m3 298.20 The impact of uni-univalent electrolytes on (water + acetic acid + toluene) equilibria: Representation with electrolyte-NRTL model
ρl 1049.42 kg/m3 298.20 (Liquid + liquid) equilibria of the (water + carboxylic acid + dibasic esters mixture (DBE-2)) ternary systems
ρl 1049.42 kg/m3 298.20 Liquid Phase Equilibria of the Water + Acetic Acid + Dimethyl Carbonate Ternary System at Several Temperatures
ρl 1041.40 kg/m3 303.15 Probe of Interactions of Acetic and Propionic Acids with 2',3'-N-Epoxypropyl-N-methyl-2-oxopyrrolidinium Salicylate Ionic Liquid
ρl 1037.00 kg/m3 303.15 Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl 1035.80 kg/m3 308.15 Probe of Interactions of Acetic and Propionic Acids with 2',3'-N-Epoxypropyl-N-methyl-2-oxopyrrolidinium Salicylate Ionic Liquid
ρl 1030.00 kg/m3 313.15 Probe of Interactions of Acetic and Propionic Acids with 2',3'-N-Epoxypropyl-N-methyl-2-oxopyrrolidinium Salicylate Ionic Liquid
ρl 1025.00 kg/m3 313.15 Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl 1028.13 kg/m3 313.20 Liquid-liquid equilibrium data for ternary systems of water + acetic acid + acetate esters at 293.2 K and 303.2 K and ~ 95 kPa
ρl 1026.72 kg/m3 313.20 The impact of uni-univalent electrolytes on (water + acetic acid + toluene) equilibria: Representation with electrolyte-NRTL model
ρl 1028.13 kg/m3 313.20 Liquid-liquid equilibrium data and thermophysical properties for ternary systems composed of water, acetic acid and different solvents
ρl 1015.00 kg/m3 323.15 Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl 1004.00 kg/m3 333.15 Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl 993.00 kg/m3 343.15 Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ΔfusS [38.36; 40.47] J/mol×K [289.90; 290.06] Show Hide
ΔfusS 40.47 J/mol×K 289.90 NIST
ΔfusS 40.47 J/mol×K 289.90 NIST
ΔfusS 38.36 J/mol×K 290.06 NIST
γ [0.02; 0.03] N/m [298.15; 343.15] Show Hide
γ 0.03 N/m 298.15 NCMS SOLV-DB
γ 0.03 N/m 303.15 Surface Tension of o-Xylene + Acetic Acid and m-Xylene + Acetic Acid Binary Mixtures from 303.15 K to 343.15 K
γ 0.03 N/m 303.20 KDB
γ 0.03 N/m 308.15 Surface Tension of o-Xylene + Acetic Acid and m-Xylene + Acetic Acid Binary Mixtures from 303.15 K to 343.15 K
γ 0.03 N/m 313.15 Surface Tension of o-Xylene + Acetic Acid and m-Xylene + Acetic Acid Binary Mixtures from 303.15 K to 343.15 K
γ 0.02 N/m 318.15 Surface Tension of o-Xylene + Acetic Acid and m-Xylene + Acetic Acid Binary Mixtures from 303.15 K to 343.15 K
γ 0.02 N/m 323.15 Surface Tension of o-Xylene + Acetic Acid and m-Xylene + Acetic Acid Binary Mixtures from 303.15 K to 343.15 K
γ 0.02 N/m 333.15 Surface Tension of o-Xylene + Acetic Acid and m-Xylene + Acetic Acid Binary Mixtures from 303.15 K to 343.15 K
γ 0.02 N/m 343.15 Surface Tension of o-Xylene + Acetic Acid and m-Xylene + Acetic Acid Binary Mixtures from 303.15 K to 343.15 K

Pressure Dependent Properties

Property Value Unit Pressure (kPa) Source
Tboil(P) [341.30; 389.58] K [17.00; 97.08] Show Hide
Tboil(P) 341.30 K 17.00 Study of Vapor-Liquid Equilibria for Acetic Acid + n-Propyl Acetate + Isopropyl Acetate Systems
Tboil(P) 342.87 K 18.47 Study of Vapor-Liquid Equilibria for Acetic Acid + n-Propyl Acetate + Isopropyl Acetate Systems
Tboil(P) 345.03 K 20.01 Study of Vapor-Liquid Equilibria for Acetic Acid + n-Propyl Acetate + Isopropyl Acetate Systems
Tboil(P) 346.41 K 21.29 Study of Vapor-Liquid Equilibria for Acetic Acid + n-Propyl Acetate + Isopropyl Acetate Systems
Tboil(P) 348.49 K 23.18 Study of Vapor-Liquid Equilibria for Acetic Acid + n-Propyl Acetate + Isopropyl Acetate Systems
Tboil(P) 350.35 K 24.92 Study of Vapor-Liquid Equilibria for Acetic Acid + n-Propyl Acetate + Isopropyl Acetate Systems
Tboil(P) 352.88 K 27.44 Study of Vapor-Liquid Equilibria for Acetic Acid + n-Propyl Acetate + Isopropyl Acetate Systems
Tboil(P) 355.01 K 29.78 Study of Vapor-Liquid Equilibria for Acetic Acid + n-Propyl Acetate + Isopropyl Acetate Systems
Tboil(P) 357.54 K 32.78 Study of Vapor-Liquid Equilibria for Acetic Acid + n-Propyl Acetate + Isopropyl Acetate Systems
Tboil(P) 359.26 K 34.97 Study of Vapor-Liquid Equilibria for Acetic Acid + n-Propyl Acetate + Isopropyl Acetate Systems
Tboil(P) 363.04 K 39.99 Study of Vapor-Liquid Equilibria for Acetic Acid + n-Propyl Acetate + Isopropyl Acetate Systems
Tboil(P) 368.56 K 48.99 Study of Vapor-Liquid Equilibria for Acetic Acid + n-Propyl Acetate + Isopropyl Acetate Systems
Tboil(P) 372.27 K 55.76 Study of Vapor-Liquid Equilibria for Acetic Acid + n-Propyl Acetate + Isopropyl Acetate Systems
Tboil(P) 374.54 K 60.04 Study of Vapor-Liquid Equilibria for Acetic Acid + n-Propyl Acetate + Isopropyl Acetate Systems
Tboil(P) 376.66 K 64.44 Study of Vapor-Liquid Equilibria for Acetic Acid + n-Propyl Acetate + Isopropyl Acetate Systems
Tboil(P) 379.05 K 69.39 Study of Vapor-Liquid Equilibria for Acetic Acid + n-Propyl Acetate + Isopropyl Acetate Systems
Tboil(P) 381.60 K 75.23 Study of Vapor-Liquid Equilibria for Acetic Acid + n-Propyl Acetate + Isopropyl Acetate Systems
Tboil(P) 383.32 K 79.98 Study of Vapor-Liquid Equilibria for Acetic Acid + n-Propyl Acetate + Isopropyl Acetate Systems
Tboil(P) 384.82 K 83.66 Study of Vapor-Liquid Equilibria for Acetic Acid + n-Propyl Acetate + Isopropyl Acetate Systems
Tboil(P) 386.07 K 87.18 Study of Vapor-Liquid Equilibria for Acetic Acid + n-Propyl Acetate + Isopropyl Acetate Systems
Tboil(P) 389.58 K 97.08 Study of Vapor-Liquid Equilibria for Acetic Acid + n-Propyl Acetate + Isopropyl Acetate Systems

Datasets

Viscosity, Pa*s

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Viscosity, Pa*s - Liquid
313.15 100.00 0.0009
313.15 800.00 0.0009
313.15 1600.00 0.0009
313.15 2400.00 0.0009
313.15 3200.00 0.0009
333.15 100.00 0.0007
333.15 800.00 0.0007
333.15 1600.00 0.0007
333.15 2400.00 0.0007
333.15 3200.00 0.0007
353.15 100.00 0.0006
353.15 800.00 0.0006
353.15 1600.00 0.0006
353.15 2400.00 0.0006
353.15 3200.00 0.0006
373.15 100.00 0.0005
373.15 800.00 0.0005
373.15 1600.00 0.0005
373.15 2400.00 0.0005
373.15 3200.00 0.0005
393.15 800.00 0.0004
393.15 1600.00 0.0004
393.15 2400.00 0.0004
393.15 3200.00 0.0004
413.15 800.00 0.0003
413.15 1600.00 0.0003
413.15 2400.00 0.0003
413.15 3200.00 0.0004
433.15 800.00 0.0003
433.15 1600.00 0.0003
433.15 2400.00 0.0003
433.15 3200.00 0.0003
453.15 800.00 0.0002
453.15 1600.00 0.0003
453.15 2400.00 0.0003
453.15 3200.00 0.0003
473.15 1600.00 0.0002
473.15 2400.00 0.0002
473.15 3200.00 0.0002
Reference

Correlations

Property Value Unit Temperature (K) Source
Cp,gas [40.11; 157.47] J/mol×K [50.00; 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 A4.01100e+01
Coefficient B-5.88240e+02
Coefficient C5.10924e+00
Coefficient D1.62490e-04
Coefficient E-8.69180e-08
Temperature range, min.50.00
Temperature range, max.1500.00
Cp,gas 40.11 J/mol×K 50.00 Calculated Property
Cp,gas 50.63 J/mol×K 211.11 Calculated Property
Cp,gas 75.89 J/mol×K 372.22 Calculated Property
Cp,gas 98.56 J/mol×K 533.33 Calculated Property
Cp,gas 116.29 J/mol×K 694.44 Calculated Property
Cp,gas 129.87 J/mol×K 855.56 Calculated Property
Cp,gas 140.19 J/mol×K 1016.67 Calculated Property
Cp,gas 147.95 J/mol×K 1177.78 Calculated Property
Cp,gas 153.59 J/mol×K 1338.89 Calculated Property
Cp,gas 157.47 J/mol×K 1500.00 Calculated Property
Property Value Unit Temperature (K) Source
Cp,liquid [122.09; 151.28] J/mol×K [289.69; 400.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is Cp,liquid in J/mol×K, T in K
Coefficient A4.90340e+01
Coefficient B1.05110e+03
Coefficient C-6.13212e+00
Coefficient D3.16670e-02
Coefficient E-2.83440e-05
Temperature range, min.289.69
Temperature range, max.400.00
Cp,liquid 122.09 J/mol×K 289.69 Calculated Property
Cp,liquid 124.72 J/mol×K 301.95 Calculated Property
Cp,liquid 127.67 J/mol×K 314.20 Calculated Property
Cp,liquid 130.88 J/mol×K 326.46 Calculated Property
Cp,liquid 134.26 J/mol×K 338.72 Calculated Property
Cp,liquid 137.75 J/mol×K 350.97 Calculated Property
Cp,liquid 141.28 J/mol×K 363.23 Calculated Property
Cp,liquid 144.76 J/mol×K 375.49 Calculated Property
Cp,liquid 148.12 J/mol×K 387.74 Calculated Property
Cp,liquid 151.28 J/mol×K 400.00 Calculated Property
Property Value Unit Temperature (K) Source
η [0.0013093; 0.0001952] Pa×s [288.15; 474.00] 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-5.85280e+01
Coefficient B2.99090e+03
Coefficient C7.49110e+00
Coefficient D-1.10280e-05
Coefficient E2.00000e+00
Temperature range, min.288.15
Temperature range, max.474.00
η 0.0013093 Pa×s 288.15 Calculated Property
η 0.0009588 Pa×s 308.80 Calculated Property
η 0.0007337 Pa×s 329.45 Calculated Property
η 0.0005802 Pa×s 350.10 Calculated Property
η 0.0004699 Pa×s 370.75 Calculated Property
η 0.0003874 Pa×s 391.40 Calculated Property
η 0.0003233 Pa×s 412.05 Calculated Property
η 0.0002721 Pa×s 432.70 Calculated Property
η 0.0002302 Pa×s 453.35 Calculated Property
η 0.0001952 Pa×s 474.00 Calculated Property
Property Value Unit Temperature (K) Source
ΔvapH [22.76; 5.26] kJ/mol [289.81; 591.95] 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 A6.62030e+01
Coefficient B6.71210e+00
Coefficient C-1.74500e+01
Coefficient D1.72000e+01
Coefficient E-6.00380e+00
Critical temperature, Tc (K)5.94450e+02
Temperature range, min.289.81
Temperature range, max.591.95
ΔvapH 22.76 kJ/mol 289.81 Calculated Property
ΔvapH 23.06 kJ/mol 323.38 Calculated Property
ΔvapH 23.35 kJ/mol 356.95 Calculated Property
ΔvapH 23.47 kJ/mol 390.52 Calculated Property
ΔvapH 23.25 kJ/mol 424.09 Calculated Property
ΔvapH 22.56 kJ/mol 457.67 Calculated Property
ΔvapH 21.23 kJ/mol 491.24 Calculated Property
ΔvapH 19.04 kJ/mol 524.81 Calculated Property
ΔvapH 15.37 kJ/mol 558.38 Calculated Property
ΔvapH 5.26 kJ/mol 591.95 Calculated Property
Property Value Unit Temperature (K) Source
Pvap [0.61; 5765.55] kPa [289.81; 591.95] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.47385e+01
Coefficient B-3.05591e+03
Coefficient C-8.92370e+01
Temperature range, min.289.81
Temperature range, max.591.95
Pvap 0.61 kPa 289.81 Calculated Property
Pvap 5.40 kPa 323.38 Calculated Property
Pvap 27.76 kPa 356.95 Calculated Property
Pvap 99.05 kPa 390.52 Calculated Property
Pvap 273.83 kPa 424.09 Calculated Property
Pvap 628.95 kPa 457.67 Calculated Property
Pvap 1257.30 kPa 491.24 Calculated Property
Pvap 2258.87 kPa 524.81 Calculated Property
Pvap 3731.87 kPa 558.38 Calculated Property
Pvap 5765.55 kPa 591.95 Calculated Property
Pvap [0.42; 5799.20] kPa [273.15; 594.45] 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 A8.05983e+01
Coefficient B-7.60391e+03
Coefficient C-9.65531e+00
Coefficient D7.16883e-06
Coefficient E2.00000e+00
CommentRange stopped at Tc; ChemSep gives it to 594.75 K.
Temperature range, min.273.15
Temperature range, max.594.45
Pvap 0.42 kPa 273.15 Calculated Property
Pvap 3.70 kPa 308.85 Calculated Property
Pvap 19.52 kPa 344.55 Calculated Property
Pvap 72.04 kPa 380.25 Calculated Property
Pvap 206.61 kPa 415.95 Calculated Property
Pvap 494.14 kPa 451.65 Calculated Property
Pvap 1034.73 kPa 487.35 Calculated Property
Pvap 1964.19 kPa 523.05 Calculated Property
Pvap 3467.03 kPa 558.75 Calculated Property
Pvap 5799.20 kPa 594.45 Calculated Property
Pvap [1.30; 5775.35] kPa [289.81; 592.71] 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 A6.82294e+01
Coefficient B-7.02972e+03
Coefficient C-7.79853e+00
Coefficient D5.93100e-06
Coefficient E0.00000e+00
Temperature range, min.289.81
Temperature range, max.592.71
Pvap 1.30 kPa 289.81 Calculated Property
Pvap 7.76 kPa 323.47 Calculated Property
Pvap 31.85 kPa 357.12 Calculated Property
Pvap 99.81 kPa 390.78 Calculated Property
Pvap 256.77 kPa 424.43 Calculated Property
Pvap 570.27 kPa 458.09 Calculated Property
Pvap 1133.54 kPa 491.74 Calculated Property
Pvap 2070.61 kPa 525.40 Calculated Property
Pvap 3545.16 kPa 559.05 Calculated Property
Pvap 5775.35 kPa 592.71 Calculated Property
Pvap [1.33; 101.33] kPa [290.26; 391.01] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.53860e+01
Coefficient B-3.78209e+03
Coefficient C-3.97640e+01
ReferenceMcDonald, Shrader, et al., 1959
Temperature range, min.290.26
Temperature range, max.391.01
Pvap 1.33 kPa 290.26 Calculated Property
Pvap 2.54 kPa 301.45 Calculated Property
Pvap 4.60 kPa 312.65 Calculated Property
Pvap 7.94 kPa 323.84 Calculated Property
Pvap 13.16 kPa 335.04 Calculated Property
Pvap 21.01 kPa 346.23 Calculated Property
Pvap 32.46 kPa 357.43 Calculated Property
Pvap 48.68 kPa 368.62 Calculated Property
Pvap 71.09 kPa 379.82 Calculated Property
Pvap 101.33 kPa 391.01 Calculated Property
Property Value Unit Temperature (K) Source
ρl [1067.84; 378.36] kg/m3 [273.15; 594.45] 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 A6.38172e+01
Coefficient B2.21740e-01
Coefficient C5.94760e+02
Coefficient D2.25660e-01
CommentRange stopped at Tc; ChemSep gives it to 594.75 K.
Temperature range, min.273.15
Temperature range, max.594.45
ρl 1067.84 kg/m3 273.15 Calculated Property
ρl 1031.78 kg/m3 308.85 Calculated Property
ρl 993.45 kg/m3 344.55 Calculated Property
ρl 952.30 kg/m3 380.25 Calculated Property
ρl 907.53 kg/m3 415.95 Calculated Property
ρl 857.86 kg/m3 451.65 Calculated Property
ρl 801.07 kg/m3 487.35 Calculated Property
ρl 732.71 kg/m3 523.05 Calculated Property
ρl 640.48 kg/m3 558.75 Calculated Property
ρl 378.36 kg/m3 594.45 Calculated Property
Property Value Unit Temperature (K) Source
γ [0.03; 0.02] N/m [289.85; 391.15] 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 A5.67311e-02
Coefficient B-9.94000e-05
Coefficient C0.00000e+00
Coefficient D0.00000e+00
Coefficient E0.00000e+00
Temperature range, min.289.85
Temperature range, max.391.15
γ 0.03 N/m 289.85 Calculated Property
γ 0.03 N/m 301.11 Calculated Property
γ 0.03 N/m 312.36 Calculated Property
γ 0.02 N/m 323.62 Calculated Property
γ 0.02 N/m 334.87 Calculated Property
γ 0.02 N/m 346.13 Calculated Property
γ 0.02 N/m 357.38 Calculated Property
γ 0.02 N/m 368.64 Calculated Property
γ 0.02 N/m 379.89 Calculated Property
γ 0.02 N/m 391.15 Calculated Property
γ [0.03; 9.03e-05] N/m [288.15; 591.95] 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-2.59130e-02
Coefficient B3.10860e+01
Coefficient C-2.82540e+00
Coefficient D3.67520e-05
Coefficient E-2.56390e-06
Temperature range, min.288.15
Temperature range, max.591.95
γ 0.03 N/m 288.15 Calculated Property
γ 0.02 N/m 321.91 Calculated Property
γ 0.02 N/m 355.66 Calculated Property
γ 0.02 N/m 389.42 Calculated Property
γ 0.02 N/m 423.17 Calculated Property
γ 0.01 N/m 456.93 Calculated Property
γ 0.01 N/m 490.68 Calculated Property
γ 0.01 N/m 524.44 Calculated Property
γ 0.00 N/m 558.19 Calculated Property
γ 9.03e-05 N/m 591.95 Calculated Property
Property Value Unit Temperature (K) Source
λgas [0.01; 0.06] W/m×K [289.81; 468.55] 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 A3.41370e-01
Coefficient B-8.05790e-01
Coefficient C-8.24300e+02
Coefficient D1.75840e+05
Temperature range, min.289.81
Temperature range, max.468.55
λgas 0.01 W/m×K 289.81 Calculated Property
λgas 0.02 W/m×K 309.67 Calculated Property
λgas 0.03 W/m×K 329.53 Calculated Property
λgas 0.04 W/m×K 349.39 Calculated Property
λgas 0.05 W/m×K 369.25 Calculated Property
λgas 0.07 W/m×K 389.11 Calculated Property
λgas 0.08 W/m×K 408.97 Calculated Property
λgas 0.08 W/m×K 428.83 Calculated Property
λgas 0.07 W/m×K 448.69 Calculated Property
λgas 0.06 W/m×K 468.55 Calculated Property
Property Value Unit Temperature (K) Source
λliquid [0.17; 0.14] W/m×K [274.09; 391.05] 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 A1.11590e-01
Coefficient B-5.31130e+02
Coefficient C1.63590e+00
Coefficient D-9.36900e-03
Coefficient E-7.19960e-07
Temperature range, min.274.09
Temperature range, max.391.05
λliquid 0.17 W/m×K 274.09 Calculated Property
λliquid 0.16 W/m×K 287.09 Calculated Property
λliquid 0.16 W/m×K 300.08 Calculated Property
λliquid 0.16 W/m×K 313.08 Calculated Property
λliquid 0.16 W/m×K 326.07 Calculated Property
λliquid 0.15 W/m×K 339.07 Calculated Property
λliquid 0.15 W/m×K 352.06 Calculated Property
λliquid 0.15 W/m×K 365.06 Calculated Property
λliquid 0.14 W/m×K 378.05 Calculated Property
λliquid 0.14 W/m×K 391.05 Calculated Property

Similar Compounds

Acetic acid-d4. MeCO2 anion. Acetic acid, sodium salt. CH3C(O)OO. Acetic acid, iodo-. Silver acetate. Acetic acid, rubidium salt. Acetic acid, chloro-. Acetic acid, fluoro-. Bromoacetic acid. ethaneperoxoic acid. Acetic acid, oxo-. Ethyl radical, 1-hydroxy. Acetic acid, hydroxy-. Acetic acid, cyano-.

Find more compounds similar to Acetic acid.

Mixtures

Find more mixtures with Acetic acid.

Sources

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