Acetic acid

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Gas phase thermochemistry data

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Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.

Data compiled as indicated in comments:
DRB - Donald R. Burgess, Jr.
GT - Glushko Thermocenter, Russian Academy of Sciences, Moscow

Quantity Value Units Method Reference Comment
Δfgas-433. ± 3.kJ/molAVGN/AAverage of 8 values; Individual data points
Quantity Value Units Method Reference Comment
gas282.84J/mol*KN/AWeltner W., 1955Other third-law entropy values at 298.15 K are 284.5 [ Chao J., 1986] and 290.37(4.18) J/mol*K [ Halford J.O., 1941].; GT

Constant pressure heat capacity of gas

Cp,gas (J/mol*K) Temperature (K) Reference Comment
39.5450.Chao J., 1986p=1 bar. Selected entropies and heat capacities differ from other statistically calculated values [ Weltner W., 1955] by 1.0-1.3 J/mol*K for S(T) and 3.1-5.4 J/mol*K for Cp(T). Please also see Chao J., 1978.; GT
40.42100.
42.74150.
48.34200.
59.38273.15
63.44 ± 0.11298.15
63.74300.
79.66400.
93.93500.
106.18600.
116.63700.
125.50800.
132.99900.
139.261000.
144.461100.
148.761200.
152.301300.
155.221400.
157.631500.

Phase change data

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Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.

Data compiled as indicated in comments:
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, Chris Muzny director
AC - William E. Acree, Jr., James S. Chickos
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
DH - Eugene S. Domalski and Elizabeth D. Hearing

Quantity Value Units Method Reference Comment
Tboil391.2 ± 0.6KAVGN/AAverage of 80 out of 90 values; Individual data points
Quantity Value Units Method Reference Comment
Tfus289.6 ± 0.5KAVGN/AAverage of 8 values; Individual data points
Quantity Value Units Method Reference Comment
Ttriple289.8KN/AWilhoit, Chao, et al., 1985Uncertainty assigned by TRC = 0.05 K; TRC
Ttriple289.69KN/AMartin and Andon, 1982Uncertainty assigned by TRC = 0.04 K; TRC
Ttriple289.8KN/AParks and Kelley, 1925Uncertainty assigned by TRC = 0.15 K; TRC
Quantity Value Units Method Reference Comment
Tc593. ± 3.KAVGN/AAverage of 10 values; Individual data points
Quantity Value Units Method Reference Comment
Pc57.81barN/AAndereya and Chase, 1990Uncertainty assigned by TRC = 0.20 bar; TRC
Pc58.2901barN/AD'Souza and Teja, 1987Uncertainty assigned by TRC = 0.90 bar; Ambrose's procedure; TRC
Pc57.86barN/AAmbrose, Ellender, et al., 1977Uncertainty assigned by TRC = 0.08 bar; TRC
Pc57.87barN/AYoung, 1910Uncertainty assigned by TRC = 1.0132 bar; TRC
Pc57.867barN/AYoung, 1891Uncertainty assigned by TRC = 0.2666 bar; TRC
Quantity Value Units Method Reference Comment
ρc5.84mol/lN/AVandana and Teja, 1995Uncertainty assigned by TRC = 0.02 mol/l; TRC
ρc5.838mol/lN/AYoung, 1910Uncertainty assigned by TRC = 0.02 mol/l; TRC
Quantity Value Units Method Reference Comment
Δvap50.3kJ/molCGCVerevkin, 2000Based on data from 303. to 378. K.; AC
Δvap51.6kJ/molN/AMajer and Svoboda, 1985 
Δvap51.6 ± 1.5kJ/molCKonicek and Wadso, 1970ALS
Δvap51.6 ± 1.6kJ/molCKonicek, Wadsö, et al., 1970AC

Enthalpy of vaporization

ΔvapH (kJ/mol) Temperature (K) Method Reference Comment
23.7391.1N/AMajer and Svoboda, 1985 
39.1360.EBMuñoz and Krähenbühl, 2001Based on data from 345. to 383. K.; AC
40.9335.N/AVercher, Vázquez, et al., 2001Based on data from 320. to 395. K.; AC
37.9406.AStephenson and Malanowski, 1987Based on data from 391. to 550. K.; AC
42.0305.AStephenson and Malanowski, 1987Based on data from 290. to 396. K.; AC
38.7406.AStephenson and Malanowski, 1987Based on data from 391. to 447. K.; AC
38.1452.AStephenson and Malanowski, 1987Based on data from 437. to 535. K.; AC
38.8540.AStephenson and Malanowski, 1987Based on data from 525. to 593. K.; AC
41.6304.AStephenson and Malanowski, 1987Based on data from 289. to 392. K. See also Dykyj, 1970.; AC
43.0308.N/ATamir, Dragoescu, et al., 1983AC
40.3340.N/AMcDonald, Shrader, et al., 1959Based on data from 325. to 391. K.; AC
41.6318.MMPotter and Ritter, 1954Based on data from 303. to 399. K.; AC

Enthalpy of vaporization

ΔvapH = A exp(-αTr) (1 − Tr)β
    ΔvapH = Enthalpy of vaporization (at saturation pressure) (kJ/mol)
    Tr = reduced temperature (T / Tc)

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Temperature (K) 298. to 392.
A (kJ/mol) 22.84
α 0.0184
β -0.0454
Tc (K) 592.7
ReferenceMajer and Svoboda, 1985

Antoine Equation Parameters

log10(P) = A − (B / (T + C))
    P = vapor pressure (bar)
    T = temperature (K)

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Temperature (K) A B C Reference
290.26 to 391.014.682061642.54-39.764McDonald, Shrader, et al., 1959

Enthalpy of sublimation

ΔsubH (kJ/mol) Temperature (K) Method Reference Comment
67. ± 1.223.TE,MECalis-Van Ginkel, Calis, et al., 1978Based on data from 213. to 230. K.; AC
70. ± 1.213.TE,MECalis-Van Ginkel, Calis, et al., 1978Based on data from 213. to 230. K.; AC

Enthalpy of fusion

ΔfusH (kJ/mol) Temperature (K) Reference Comment
11.72298.7Domalski and Hearing, 1996See also Martin and Andon, 1982, 2.; AC
11.728289.9Parks and Kelley, 1925, 2DH
10.83289.8Louguinine and Dupont, 1911AC
11.52283.7Meyer, 1910AC
11.126290.06Pickering, 1895DH

Entropy of fusion

ΔfusS (J/mol*K) Temperature (K) Reference Comment
40.47289.9Parks and Kelley, 1925, 2DH
38.36290.06Pickering, 1895DH

Enthalpy of phase transition

ΔHtrs (kJ/mol) Temperature (K) Initial Phase Final Phase Reference Comment
11.720298.69crystaline, IliquidMartin and Andon, 1982, 2DH

Entropy of phase transition

ΔStrs (J/mol*K) Temperature (K) Initial Phase Final Phase Reference Comment
40.5298.69crystaline, IliquidMartin and Andon, 1982, 2DH

In addition to the Thermodynamics Research Center (TRC) data available from this site, much more physical and chemical property data is available from the following TRC products:


References

Go To: Top, Gas phase thermochemistry data, Phase change data, Notes

Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.

Weltner W., 1955
Weltner W., Jr., The vibrational spectrum, associative and thermodynamic properties of acetic acid vapor, J. Am. Chem. Soc., 1955, 77, 3941-3950. [all data]

Chao J., 1986
Chao J., Thermodynamic properties of key organic oxygen compounds in the carbon range C1 to C4. Part 2. Ideal gas properties, J. Phys. Chem. Ref. Data, 1986, 15, 1369-1436. [all data]

Halford J.O., 1941
Halford J.O., The entropy of acetic acid, J. Chem. Phys., 1941, 9, 859-863. [all data]

Chao J., 1978
Chao J., Ideal gas thermodynamic properties of methanoic and ethanoic acids, J. Phys. Chem. Ref. Data, 1978, 7, 363-377. [all data]

Wilhoit, Chao, et al., 1985
Wilhoit, R.C.; Chao, J.; Hall, K.R., Thermodynamic Properties of Key Organic Compounds in the Carbon Range C1 to C4. Part 1. Properties of Condensed Phases, J. Phys. Chem. Ref. Data, 1985, 14, 1. [all data]

Martin and Andon, 1982
Martin, J.F.; Andon, R.J.L., Thermodynamic properties of organic oxygen compounds. Part LII. Molar heat capacity of ethanoic, propanoic, and butanoic acids., J. Chem. Thermodyn., 1982, 14, 679-88. [all data]

Parks and Kelley, 1925
Parks, G.S.; Kelley, K.K., Thermal Data on Organic Compounds II. The Heat Capacities of Five Organic Compounds. The Entropies and Free Energies of Some Homologous Series of Aliphatic Compounds, J. Am. Chem. Soc., 1925, 47, 2089-97. [all data]

Andereya and Chase, 1990
Andereya, E.; Chase, J.D., Chem. Eng. Technol., 1990, 13, 304-12. [all data]

D'Souza and Teja, 1987
D'Souza, R.; Teja, A.S., The prediction of the vapor pressures of carboxylic acids, Chem. Eng. Commun., 1987, 61, 13. [all data]

Ambrose, Ellender, et al., 1977
Ambrose, D.; Ellender, J.H.; Sprake, C.H.S.; Townsend, R., Thermo. Prop. of Org. Oxygen Compounds XLV. The Vapor Pressure of Acetic Acid, J. Chem. Thermodyn., 1977, 9, 735. [all data]

Young, 1910
Young, S., The Internal Heat of Vaporization constants of thirty pure substances, Sci. Proc. R. Dublin Soc., 1910, 12, 374. [all data]

Young, 1891
Young, S., J. Chem. Soc., 1891, 59, 903. [all data]

Vandana and Teja, 1995
Vandana, V.; Teja, A.S., The critical temperatures and densities of acetic acid-water mixtures, Fluid Phase Equilib., 1995, 103, 113-18. [all data]

Verevkin, 2000
Verevkin, S.P., Measurement and Prediction of the Monocarboxylic Acids Thermochemical Properties, J. Chem. Eng. Data, 2000, 45, 5, 953-960, https://doi.org/10.1021/je990282m . [all data]

Majer and Svoboda, 1985
Majer, V.; Svoboda, V., Enthalpies of Vaporization of Organic Compounds: A Critical Review and Data Compilation, Blackwell Scientific Publications, Oxford, 1985, 300. [all data]

Konicek and Wadso, 1970
Konicek, J.; Wadso, I., Enthalpies of vaporization of organic compounds. VII. Some carboxylic acids, Acta Chem. Scand., 1970, 24, 2612-26. [all data]

Konicek, Wadsö, et al., 1970
Konicek, Jiri; Wadsö, Ingemar; Munch-Petersen, J.; Ohlson, Ragnar; Shimizu, Akira, Enthalpies of Vaporization of Organic Compounds. VII. Some Carboxylic Acids., Acta Chem. Scand., 1970, 24, 2612-2616, https://doi.org/10.3891/acta.chem.scand.24-2612 . [all data]

Muñoz and Krähenbühl, 2001
Muñoz, Laura A.L.; Krähenbühl, M. Alvina, Isobaric Vapor Liquid Equilibrium (VLE) Data of the Systems n -Butanol + Butyric Acid and n -Butanol + Acetic Acid, J. Chem. Eng. Data, 2001, 46, 1, 120-124, https://doi.org/10.1021/je000033u . [all data]

Vercher, Vázquez, et al., 2001
Vercher, Ernesto; Vázquez, M. Isabel; Martínez-Andreu, Antoni, Isobaric Vapor-Liquid Equilibria for Water + Acetic Acid + Lithium Acetate, J. Chem. Eng. Data, 2001, 46, 6, 1584-1588, https://doi.org/10.1021/je010106p . [all data]

Stephenson and Malanowski, 1987
Stephenson, Richard M.; Malanowski, Stanislaw, Handbook of the Thermodynamics of Organic Compounds, 1987, https://doi.org/10.1007/978-94-009-3173-2 . [all data]

Dykyj, 1970
Dykyj, J., Petrochemica, 1970, 10, 2, 51. [all data]

Tamir, Dragoescu, et al., 1983
Tamir, Abraham; Dragoescu, Claudia; Apelblat, Alexander; Wisniak, Jaime, Heats of vaporization and vapor-liquid equilibria in associated solutions containing formic acid, acetic acid, propionic acid and carbon tetrachloride, Fluid Phase Equilibria, 1983, 10, 1, 9-42, https://doi.org/10.1016/0378-3812(83)80002-8 . [all data]

McDonald, Shrader, et al., 1959
McDonald, R.A.; Shrader, S.A.; Stull, D.R., Vapor Pressures and Freezing Points of Thirty Pure Organic Compounds., J. Chem. Eng. Data, 1959, 4, 4, 311-313, https://doi.org/10.1021/je60004a009 . [all data]

Potter and Ritter, 1954
Potter, Andrew E.; Ritter, H.L., The Vapor Pressure of Acetic Acid and Acetic-d 3 Acid-d. The Liquid Density of Acetic-d 3 Acid-d, J. Phys. Chem., 1954, 58, 11, 1040-1042, https://doi.org/10.1021/j150521a025 . [all data]

Calis-Van Ginkel, Calis, et al., 1978
Calis-Van Ginkel, C.H.D.; Calis, G.H.M.; Timmermans, C.W.M.; de Kruif, C.G.; Oonk, H.A.J., Enthalpies of sublimation and dimerization in the vapour phase of formic, acetic, propanoic, and butanoic acids, The Journal of Chemical Thermodynamics, 1978, 10, 11, 1083-1088, https://doi.org/10.1016/0021-9614(78)90082-4 . [all data]

Domalski and Hearing, 1996
Domalski, Eugene S.; Hearing, Elizabeth D., Heat Capacities and Entropies of Organic Compounds in the Condensed Phase. Volume III, J. Phys. Chem. Ref. Data, 1996, 25, 1, 1, https://doi.org/10.1063/1.555985 . [all data]

Martin and Andon, 1982, 2
Martin, J.F.; Andon, R.J.L., Thermodynamic properties of organic oxygen compounds. Part LII. Molar heat capacity of ethanoic, propanoic, and butanoic acids, J. Chem. Thermodynam., 1982, 14, 679-688. [all data]

Parks and Kelley, 1925, 2
Parks, G.S.; Kelley, K.K., Thermal data on organic compounds. II. The heat capacities of five organic compounds. The entropies and free energies of some homologous series of aliphatic compounds, J. Am. Chem. Soc., 1925, 47, 2089-2097. [all data]

Louguinine and Dupont, 1911
Louguinine, W.; Dupont, G., Bull. Soc. Chim. Fr., 1911, 9, 219. [all data]

Meyer, 1910
Meyer, J., Z. Phys. Chem., Stoechiom. Verwandtschaftsl., 1910, 72, 225. [all data]

Pickering, 1895
Pickering, S.U., A comparison of some properties of acetic acid and its chloro- and bromo-derivatives, J. Chem. Soc., 1895, 67, 664-684. [all data]


Notes

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