Acetone

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Gas phase thermochemistry data

Go To: Top, Phase change data, Henry's Law data, Gas phase ion energetics data, References, Notes

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:
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
GT - Glushko Thermocenter, Russian Academy of Sciences, Moscow

Quantity Value Units Method Reference Comment
Δfgas-52.23 ± 0.14kcal/molCmWiberg, Crocker, et al., 1991ALS
Δfgas-51.90 ± 0.12kcal/molCmChao and Zwolinski, 1976ALS
Δfgas-51.99 ± 0.16kcal/molEqkBuckley and Herington, 1965ALS
Δfgas-51.72kcal/molCmPennington and Kobe, 1957ALS
Quantity Value Units Method Reference Comment
Δcgas-435.32 ± 0.20kcal/molCcbMiles and Hunt, 1941Corresponding Δfgas = -51.78 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS

Constant pressure heat capacity of gas

Cp,gas (cal/mol*K) Temperature (K) Reference Comment
12.36100.Chao J., 1986p=1 bar. Recommended values agree with results of statistical calculations [ Pennington R.E., 1957, Chao J., 1976] within 0.5-2.8 J/mol*K.; GT
13.43150.
14.63200.
16.99273.15
17.93 ± 0.026298.15
18.00300.
22.00400.
25.832500.
29.207600.
32.130700.
34.656800.
36.843900.
38.7401000.
40.3821100.
41.8071200.
43.0431300.
44.1161400.
45.0501500.

Constant pressure heat capacity of gas

Cp,gas (cal/mol*K) Temperature (K) Reference Comment
19.26 ± 0.19332.6Chao J., 1976Experimental data [ Vilcu R., 1975] differ substantially from data selected here. Their correctness seems to be doubtful (see [ Kabo G.J., 1995]). Please also see Bennewitz K., 1938, Collins B.T., 1949, Pennington R.E., 1957.; GT
19.35 ± 0.19334.
19.48 ± 0.038338.2
19.92 ± 0.20347.8
19.93 ± 0.20348.
20.80 ± 0.21363.
20.84 ± 0.041371.2
20.92 ± 0.21372.3
21.33 ± 0.21378.
21.95 ± 0.22393.
22.21 ± 0.045405.2
22.51 ± 0.22408.
22.30410.
23.13 ± 0.46422.6
23.76 ± 0.48428.
24.02 ± 0.48438.
23.58 ± 0.048439.2

Phase change data

Go To: Top, Gas phase thermochemistry data, Henry's Law data, Gas phase ion energetics data, References, Notes

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
BS - Robert L. Brown and Stephen E. Stein
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
Tboil329.3 ± 0.3KAVGN/AAverage of 117 out of 129 values; Individual data points
Quantity Value Units Method Reference Comment
Tfus178.7 ± 0.9KAVGN/AAverage of 11 values; Individual data points
Quantity Value Units Method Reference Comment
Ttriple178.5KN/AWilhoit, Chao, et al., 1985Uncertainty assigned by TRC = 0.3 K; TRC
Ttriple176.6KN/AKelley, 1929Crystal phase 1 phase; Uncertainty assigned by TRC = 0.15 K; deduced from appearance of a small maximum in heat capacity; TRC
Ttriple177.6KN/AParks and Kelley, 1928Uncertainty assigned by TRC = 0.3 K; TRC
Ttriple177.6KN/AParks and Kelley, 1925Uncertainty assigned by TRC = 0.2 K; TRC
Quantity Value Units Method Reference Comment
Tc508. ± 2.KAVGN/AAverage of 19 values; Individual data points
Quantity Value Units Method Reference Comment
Pc48. ± 4.atmAVGN/AAverage of 9 values; Individual data points
Quantity Value Units Method Reference Comment
ρc4.63mol/lN/ACampbell and Chatterjee, 1969Uncertainty assigned by TRC = 0.05 mol/l; TRC
ρc4.03mol/lN/ACampbell and Chatterjee, 1968Uncertainty assigned by TRC = 0.026 mol/l; TRC
ρc4.79mol/lN/AKobe, Crawford, et al., 1955Uncertainty assigned by TRC = 0.17 mol/l; TRC
ρc4.70mol/lN/ARosenbaum, 1951Uncertainty assigned by TRC = 0.02 mol/l; TRC
ρc4.34mol/lN/AHerz and Neukirch, 1923Uncertainty assigned by TRC = 0.03 mol/l; TRC
Quantity Value Units Method Reference Comment
Δvap7.474kcal/molN/AMajer and Svoboda, 1985 
Δvap7.48kcal/molN/AAmbrose, Ellender, et al., 1975AC
Δvap7.09 ± 0.001kcal/molVMathews, 1926ALS

Reduced pressure boiling point

Tboil (K) Pressure (atm) Reference Comment
329.30.026Buckingham and Donaghy, 1982BS

Enthalpy of vaporization

ΔvapH (kcal/mol) Temperature (K) Method Reference Comment
6.96329.3N/AMajer and Svoboda, 1985 
7.67308.N/ASoni, Ramjugernath, et al., 2008Based on data from 298. to 318. K.; AC
7.15344.AStephenson and Malanowski, 1987Based on data from 329. to 488. K.; AC
7.86228.AStephenson and Malanowski, 1987Based on data from 178. to 243. K.; AC
8.08254.AStephenson and Malanowski, 1987Based on data from 203. to 269. K.; AC
7.31338.AStephenson and Malanowski, 1987Based on data from 323. to 379. K.; AC
7.05389.AStephenson and Malanowski, 1987Based on data from 374. to 464. K.; AC
7.10472.AStephenson and Malanowski, 1987Based on data from 457. to 508. K.; AC
7.84274.AStephenson and Malanowski, 1987Based on data from 259. to 351. K. See also Ambrose, Sprake, et al., 1974 and Ambrose, Ellender, et al., 1975.; AC
7.82276.A,EBStephenson and Malanowski, 1987Based on data from 261. to 328. K. See also Boublík and Aim, 1972.; AC
7.62300.EBBaliah and Gnanasekaran, 1986Based on data from 285. to 329. K.; AC
6.24373.CDmitriev, Kachurina, et al., 1986AC
5.19423.CDmitriev, Kachurina, et al., 1986AC
3.66473.CDmitriev, Kachurina, et al., 1986AC
2.2498.CDmitriev, Kachurina, et al., 1986AC
7.60319.N/ACastellari, Francesconi, et al., 1984Based on data from 305. to 333. K.; AC
7.79285.N/ASokolov, Zhilina, et al., 1963Based on data from 278. to 293. K.; AC
7.43319.N/ABrown and Smith, 1957Based on data from 310. to 329. K.; AC
6.952338.CPennington and Kobe, 1957ALS
8.4253.MGFelsing and Durban, 1926Based on data from 204. to 339. K.; AC
7.67293.MGFelsing and Durban, 1926Based on data from 204. to 339. K.; AC
7.34313.MGFelsing and Durban, 1926Based on data from 204. to 339. K.; AC

Enthalpy of vaporization

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

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Temperature (K) A (kcal/mol) β Tc (K) Reference Comment
300. to 345.11.220.2826508.2Majer and Svoboda, 1985 

Antoine Equation Parameters

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

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Temperature (K) A B C Reference Comment
259.16 to 507.604.418771312.253-32.445Ambrose, Sprake, et al., 1974Coefficents calculated by NIST from author's data.

Enthalpy of fusion

ΔfusH (kcal/mol) Temperature (K) Reference Comment
1.366176.62Kelley, 1929, 2DH
1.37176.6Domalski and Hearing, 1996AC
1.360177.6Parks and Kelley, 1928, 2DH
1.140178.5Maass and Walbauer, 1925DH
1.360177.6Parks and Kelley, 1925, 2DH

Entropy of fusion

ΔfusS (cal/mol*K) Temperature (K) Reference Comment
7.734176.62Kelley, 1929, 2DH
7.65177.6Parks and Kelley, 1928, 2DH
6.38178.5Maass and Walbauer, 1925DH
7.655177.6Parks and Kelley, 1925, 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:


Henry's Law data

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

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

Data compiled by: Rolf Sander

Henry's Law constant (water solution)

kH(T) = H exp(d(ln(kH))/d(1/T) ((1/T) - 1/(298.15 K)))
H = Henry's law constant for solubility in water at 298.15 K (mol/(kg*bar))
d(ln(kH))/d(1/T) = Temperature dependence constant (K)

H (mol/(kg*bar)) d(ln(kH))/d(1/T) (K) Method Reference Comment
30.4600.LN/A 
27.5300.MN/A 
27. MN/A 
23. QN/A missing citation give several references for the Henry's law constants but don't assign them to specific species.
32.5800.MN/A 
35.3800.MN/AThe data from Table 1 by missing citation was used to redo the regression analysis. The data for acetone in their Table 2 is wrong.
3.03300.XN/A 
26.4800.MN/A 
30. XN/AValue given here as quoted by missing citation.
25. MN/A 
25. XN/AValue given here as quoted by missing citation.
25. MButtery, Ling, et al., 1969 
22.5000.XN/A 
3.1 RN/A 
28. MN/A 
30. RN/A 

Gas phase ion energetics data

Go To: Top, Gas phase thermochemistry data, Phase change data, Henry's Law data, References, Notes

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

Data evaluated as indicated in comments:
HL - Edward P. Hunter and Sharon G. Lias
L - Sharon G. Lias

Data compiled as indicated in comments:
B - John E. Bartmess
MM - Michael M. Meot-Ner (Mautner)
LBLHLM - Sharon G. Lias, John E. Bartmess, Joel F. Liebman, John L. Holmes, Rhoda D. Levin, and W. Gary Mallard
LLK - Sharon G. Lias, Rhoda D. Levin, and Sherif A. Kafafi
RDSH - Henry M. Rosenstock, Keith Draxl, Bruce W. Steiner, and John T. Herron

View reactions leading to C3H6O+ (ion structure unspecified)

Quantity Value Units Method Reference Comment
IE (evaluated)9.703 ± 0.006eVN/AN/AL
Quantity Value Units Method Reference Comment
Proton affinity (review)194.kcal/molN/AHunter and Lias, 1998HL
Quantity Value Units Method Reference Comment
Gas basicity186.9kcal/molN/AHunter and Lias, 1998HL

Electron affinity determinations

EA (eV) Method Reference Comment
0.00152EFDDesfrancois, Abdoul-Carime, et al., 1994EA: 1.5 meV. Dipole-bound state.; B

Proton affinity at 298K

Proton affinity (kcal/mol) Reference Comment
>194.8Bouchoux, Buisson, et al., 2003MM
>194.6Bouchoux, Buisson, et al., 2003MM
>194.2 ± 0.05Bouchoux, Buisson, et al., 2003MM
194.0 ± 0.81Bouchoux and Salpin, 1999T = 301K; Re-evaluated thermokinetic parametric fitting by the authors using reference base GBs and PAs from Hunter and Lias, 1998; MM
194.0 ± 0.81Bouchoux and Salpin, 1999T = 298K; MM

Gas basicity at 298K

Gas basicity (review) (kcal/mol) Reference Comment
187.5Bouchoux, Buisson, et al., 2003MM
187.0Bouchoux, Buisson, et al., 2003MM
186.9 ± 0.05Bouchoux, Buisson, et al., 2003MM
186.9 ± 0.36Bouchoux and Salpin, 1999T = 301K; Re-evaluated thermokinetic parametric fitting by the authors using reference base GBs and PAs from Hunter and Lias, 1998; MM
186.9 ± 0.36Bouchoux and Salpin, 1999T = 298K; MM

Ionization energy determinations

IE (eV) Method Reference Comment
9.70PITraeger, McLouglin, et al., 1982LBLHLM
9.694 ± 0.006PITrott, Blais, et al., 1978LLK
9.68PIStaley, Wieting, et al., 1977LLK
9.709 ± 0.005PEHernandez, Masclet, et al., 1977LLK
9.71 ± 0.03EIMouvier and Hernandez, 1975LLK
9.71 ± 0.01PEMouvier and Hernandez, 1975LLK
9.71PETam, Yee, et al., 1974LLK
9.71SOgata, Kitayama, et al., 1974LLK
9.700 ± 0.001PIKnowles and Nicholson, 1974LLK
9.705SHuebner, Celotta, et al., 1973LLK
9.71 ± 0.01PIPotapov and Sorokin, 1972LLK
9.75 ± 0.025PEJohnstone and Mellon, 1972LLK
9.72PEBrundle, Robin, et al., 1972LLK
9.74EIJohnstone, Mellon, et al., 1971LLK
9.71 ± 0.01PECocksey, Eland, et al., 1971LLK
9.74 ± 0.03EIJohnstone, Mellon, et al., 1970RDSH
9.68PEDewar and Worley, 1969RDSH
9.71 ± 0.01PIPotapov, Filyugina, et al., 1968RDSH
9.7 ± 0.1EIDorman, 1965RDSH
9.68 ± 0.02PIMurad and Inghram, 1964RDSH
9.67PEAl-Joboury and Turner, 1964RDSH
9.71 ± 0.03PIVilesov, 1960RDSH
9.71 ± 0.03PIVilesov and Terenin, 1957RDSH
9.69 ± 0.01PIWatanabe, 1954RDSH
9.705SWatanabe, 1954RDSH
9.8PEBieri, Asbrink, et al., 1982Vertical value; LBLHLM
9.72PEKobayashi, 1978Vertical value; LLK
9.68PEBenoit and Harrison, 1977Vertical value; LLK
9.71 ± 0.02PEYoung and Cheng, 1976Vertical value; LLK
9.5PERao, 1975Vertical value; LLK
9.70PEKimura, Katsumata, et al., 1975Vertical value; LLK
9.709PEAue, Webb, et al., 1975Vertical value; LLK
9.71PEKelder, Cerfontain, et al., 1974Vertical value; LLK
9.72PEHentrich, Gunkel, et al., 1974Vertical value; LLK

Appearance energy determinations

Ion AE (eV) Other Products MethodReferenceComment
CH3+15.61?PEPowis and Danby, 1979LLK
CH3+15.2?EIMajer, Olavesen, et al., 1971LLK
CH3+14.93?EIPotzinger and Bunau, 1969RDSH
CH3+15.36?EIHaney and Franklin, 1969RDSH
C2H2O+10.7 ± 0.1CH4EIShigorin, Filyugina, et al., 1966RDSH
C2H3+16.9?EIKanomata, 1961RDSH
C2H3O+10.38CH3PITraeger, McLouglin, et al., 1982LBLHLM
C2H3O+12.22CH3PEPowis and Danby, 1979LLK
C2H3O+10.52 ± 0.02CH3PITrott, Blais, et al., 1978LLK
C2H3O+10.36CH3PIStaley, Wieting, et al., 1977LLK
C2H3O+10.30CH3EIMouvier and Hernandez, 1975LLK
C2H3O+10.42 ± 0.03CH3PIPotapov and Sorokin, 1972LLK
C2H3O+10.28 ± 0.05CH3EIJohnstone and Mellon, 1972LLK
C2H3O+11.3CH3EIMajer, Olavesen, et al., 1971LLK
C2H3O+10.28CH3EIJohnstone, Mellon, et al., 1970RDSH
C2H3O+10.42CH3PIPotapov, Filyugina, et al., 1968RDSH
C2H3O+10.2 ± 0.1CH3EIDorman, 1965RDSH
C2H3O+10.37CH3PIMurad and Inghram, 1964, 2RDSH
C3H4O+15.2 ± 0.15H2EIShigorin, Filyugina, et al., 1966RDSH
C3H5O+13.1 ± 0.2HEIPotapov and Shigorin, 1966RDSH

De-protonation reactions

C3H5O- + Hydrogen cation = Acetone

By formula: C3H5O- + H+ = C3H6O

Quantity Value Units Method Reference Comment
Δr368.8 ± 2.1kcal/molD-EABrinkman, Berger, et al., 1993gas phase; B
Δr369.0 ± 2.1kcal/molG+TSBartmess, Scott, et al., 1979gas phase; value altered from reference due to change in acidity scale; B
Δr369.6 ± 2.6kcal/molG+TSCumming and Kebarle, 1978gas phase; B
Δr367.6 ± 1.8kcal/molEIAEMuftakhov, Vasil'ev, et al., 1999gas phase; B
Quantity Value Units Method Reference Comment
Δr361.9 ± 2.0kcal/molIMREBartmess, Scott, et al., 1979gas phase; value altered from reference due to change in acidity scale; B
Δr362.4 ± 2.0kcal/molIMRECumming and Kebarle, 1978gas phase; B

References

Go To: Top, Gas phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics data, Notes

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

Wiberg, Crocker, et al., 1991
Wiberg, K.B.; Crocker, L.S.; Morgan, K.M., Thermochemical studies of carbonyl compounds. 5. Enthalpies of reduction of carbonyl groups, J. Am. Chem. Soc., 1991, 113, 3447-3450. [all data]

Chao and Zwolinski, 1976
Chao, J.; Zwolinski, B.J., Ideal gas thermodynamic properties of propanone and 2-butanone, J. Phys. Chem. Ref. Data, 1976, 5, 319-328. [all data]

Buckley and Herington, 1965
Buckley, E.; Herington, E.F.G., Equilibria in some secondary alcohol + hydrogen + ketone systems, Trans. Faraday Soc., 1965, 61, 1618-1625. [all data]

Pennington and Kobe, 1957
Pennington, R.E.; Kobe, K.A., The thermodynamic properties of acetone, J. Am. Chem. Soc., 1957, 79, 300-305. [all data]

Miles and Hunt, 1941
Miles, C.B.; Hunt, H., Heats of combustion. I. The heat of combustion of acetone, J. Phys. Chem., 1941, 45, 1346-1359. [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]

Pennington R.E., 1957
Pennington R.E., The thermodynamic properties of acetone, J. Am. Chem. Soc., 1957, 79, 300-305. [all data]

Chao J., 1976
Chao J., Ideal gas thermodynamic properties of propanone and 2-butanone, J. Phys. Chem. Ref. Data, 1976, 5, 319-328. [all data]

Vilcu R., 1975
Vilcu R., Determination of heat capacities of some alcohols and ketones in vapor phase, Rev. Roum. Chim., 1975, 20, 603-609. [all data]

Kabo G.J., 1995
Kabo G.J., Thermodynamic properties, conformation, and phase transitions of cyclopentanol, J. Chem. Thermodyn., 1995, 27, 953-967. [all data]

Bennewitz K., 1938
Bennewitz K., Molar heats of vapor organic compounds, Z. Phys. Chem. (Leipzig), 1938, B39, 126-144. [all data]

Collins B.T., 1949
Collins B.T., The heat capacity of organic vapors. VI. Acetone, J. Am. Chem. Soc., 1949, 71, 2929-2930. [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]

Kelley, 1929
Kelley, K.K., The heat capacities of isopropyl alcohol and acetone from 16 to 298 K and the corresponding entropies and free energies, J. Am. Chem. Soc., 1929, 51, 1145-51. [all data]

Parks and Kelley, 1928
Parks, G.S.; Kelley, K.K., The application of the third law of thermodynamics to some organic reactions, J. Phys. Chem., 1928, 32, 734-50. [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]

Campbell and Chatterjee, 1969
Campbell, A.N.; Chatterjee, R.M., The critical constants and orthobaric densities of acetone, chloroform benzene, and carbon tetrachloride, Can. J. Chem., 1969, 47, 3893-8. [all data]

Campbell and Chatterjee, 1968
Campbell, A.N.; Chatterjee, R.M., Orthobaric Data of Certain Pure Liquids in the Neighborhood of the Critical Point, Can. J. Chem., 1968, 46, 575-81. [all data]

Kobe, Crawford, et al., 1955
Kobe, K.A.; Crawford, H.R.; Stephenson, R.W., Critical Properties and Vapor Pressures of Some Ketones, Ind. Eng. Chem., 1955, 47, 1767-72. [all data]

Rosenbaum, 1951
Rosenbaum, M., , M.S. Thesis, Univ. Tex., Austin, TX, 1951. [all data]

Herz and Neukirch, 1923
Herz, W.; Neukirch, E., On Knowldge of the Critical State, Z. Phys. Chem., Stoechiom. Verwandtschaftsl., 1923, 104, 433-50. [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]

Ambrose, Ellender, et al., 1975
Ambrose, D.; Ellender, J.H.; Lees, E.B.; Sprake, C.H.S.; Townsend, R., Thermodynamic properties of organic oxygen compounds XXXVIII. Vapour pressures of some aliphatic ketones, The Journal of Chemical Thermodynamics, 1975, 7, 5, 453-472, https://doi.org/10.1016/0021-9614(75)90275-X . [all data]

Mathews, 1926
Mathews, J.H., The accurate measurement of heats of vaporization of liquids, J. Am. Chem. Soc., 1926, 48, 562-576. [all data]

Buckingham and Donaghy, 1982
Buckingham, J.; Donaghy, S.M., Dictionary of Organic Compounds: Fifth Edition, Chapman and Hall, New York, 1982, 1. [all data]

Soni, Ramjugernath, et al., 2008
Soni, Minal; Ramjugernath, Deresh; Raal, J. David, Vapor--Liquid Equilibrium for Binary Systems of 2,3-Pentanedione with Diacetyl and Acetone, J. Chem. Eng. Data, 2008, 53, 3, 745-749, https://doi.org/10.1021/je7005924 . [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]

Ambrose, Sprake, et al., 1974
Ambrose, D.; Sprake, C.H.S.; Townsend, R., Thermodynamic properties of organic oxygen compounds XXXIII. The vapour pressure of acetone, The Journal of Chemical Thermodynamics, 1974, 6, 7, 693-700, https://doi.org/10.1016/0021-9614(74)90119-0 . [all data]

Boublík and Aim, 1972
Boublík, T.; Aim, K., Heats of vaporization of simple non-spherical molecule compounds, Collect. Czech. Chem. Commun., 1972, 37, 11, 3513-3521, https://doi.org/10.1135/cccc19723513 . [all data]

Baliah and Gnanasekaran, 1986
Baliah, V.; Gnanasekaran, K., Search for hydrogen bonding in thiophenols through heats of vaporization measurements, Indian J. Chem., Sect A, 1986, 25, 7, 673. [all data]

Dmitriev, Kachurina, et al., 1986
Dmitriev, Yu.G.; Kachurina, N.S.; Wang, C.H.; Kochubei, V.V., Thermochemical properties of complex glycidol esters, Vestn. L'vov. Politekh. Inst., 1986, 201, 29. [all data]

Castellari, Francesconi, et al., 1984
Castellari, Carlo; Francesconi, Romolo; Comelli, Fabio; Ottani, Stefano, Vapor-liquid equilibria in binary systems containing 1,3-dioxolane at isobaric conditions. 6. Binary mixtures of 1,3-dioxolane with acetone, J. Chem. Eng. Data, 1984, 29, 3, 283-284, https://doi.org/10.1021/je00037a016 . [all data]

Sokolov, Zhilina, et al., 1963
Sokolov, V.V.; Zhilina, L.P.; Mischenko, K.P., Zh. Prikl. Khim. (Leningrad), 1963, 36, 750. [all data]

Brown and Smith, 1957
Brown, I.; Smith, F., Liquid-vapour equilibria viii. The systems acetoke +benzene and acetone +carbon tetrachloride at 45«65533»C, Aust. J. Chem., 1957, 10, 4, 423-621, https://doi.org/10.1071/CH9570423 . [all data]

Felsing and Durban, 1926
Felsing, W.A.; Durban, S.A., THE VAPOR PRESSURES, DENSITIES, AND SOME DERIVED QUANTITIES FOR ACETONE, J. Am. Chem. Soc., 1926, 48, 11, 2885-2893, https://doi.org/10.1021/ja01690a020 . [all data]

Kelley, 1929, 2
Kelley, K.K., The heats capacities of isopropyl alcohol and acetone from 16 to 298 °K and the corresponding entropies and free energies, J. Am. Chem. Soc., 1929, 51, 1145-1150. [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]

Parks and Kelley, 1928, 2
Parks, G.S.; Kelley, K.K., The application of the third law of thermodynamics to some organic reactions, J. Phys. Chem., 1928, 32, 734-750. [all data]

Maass and Walbauer, 1925
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Notes

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