Acetone
- Formula: C3H6O
- Molecular weight: 58.0791
- IUPAC Standard InChIKey: CSCPPACGZOOCGX-UHFFFAOYSA-N
- CAS Registry Number: 67-64-1
- Chemical structure:
This structure is also available as a 2d Mol file or as a computed 3d SD file
The 3d structure may be viewed using Java or Javascript. - Isotopologues:
- Other names: 2-Propanone; β-Ketopropane; Dimethyl ketone; Dimethylformaldehyde; Methyl ketone; Propanone; Pyroacetic ether; (CH3)2CO; Dimethylketal; Ketone propane; Ketone, dimethyl-; Chevron acetone; Rcra waste number U002; UN 1090; Sasetone; Propan-2-one; NSC 135802
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Gas phase thermochemistry data
Go To: Top, Condensed phase thermochemistry data, 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 |
---|---|---|---|---|---|
ΔfH°gas | -218.5 ± 0.59 | kJ/mol | Cm | Wiberg, Crocker, et al., 1991 | ALS |
ΔfH°gas | -217.1 ± 0.50 | kJ/mol | Cm | Chao and Zwolinski, 1976 | ALS |
ΔfH°gas | -217.5 ± 0.67 | kJ/mol | Eqk | Buckley and Herington, 1965 | ALS |
ΔfH°gas | -216.4 | kJ/mol | Cm | Pennington and Kobe, 1957 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°gas | -1821.4 ± 0.84 | kJ/mol | Ccb | Miles and Hunt, 1941 | Corresponding ΔfHºgas = -216.6 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
51.73 | 100. | Chao J., 1986 | p=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 |
56.18 | 150. | ||
61.20 | 200. | ||
71.09 | 273.15 | ||
75.02 ± 0.11 | 298.15 | ||
75.32 | 300. | ||
92.06 | 400. | ||
108.08 | 500. | ||
122.20 | 600. | ||
134.43 | 700. | ||
145.00 | 800. | ||
154.15 | 900. | ||
162.09 | 1000. | ||
168.96 | 1100. | ||
174.92 | 1200. | ||
180.09 | 1300. | ||
184.58 | 1400. | ||
188.49 | 1500. |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
80.58 ± 0.81 | 332.6 | Chao J., 1976 | Experimental 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 |
80.96 ± 0.81 | 334. | ||
81.50 ± 0.16 | 338.2 | ||
83.35 ± 0.83 | 347.8 | ||
83.39 ± 0.83 | 348. | ||
87.03 ± 0.87 | 363. | ||
87.19 ± 0.17 | 371.2 | ||
87.53 ± 0.88 | 372.3 | ||
89.24 ± 0.89 | 378. | ||
91.84 ± 0.92 | 393. | ||
92.93 ± 0.19 | 405.2 | ||
94.18 ± 0.94 | 408. | ||
93.30 | 410. | ||
96.8 ± 1.9 | 422.6 | ||
99.4 ± 2.0 | 428. | ||
100.5 ± 2.0 | 438. | ||
98.66 ± 0.20 | 439.2 |
Condensed 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:
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 |
---|---|---|---|---|---|
ΔfH°liquid | -249.4 ± 0.63 | kJ/mol | Cm | Wiberg, Crocker, et al., 1991 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -1772. | kJ/mol | Ccb | Guinchant, 1918 | Corresponding ΔfHºliquid = -267. kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -1804.2 | kJ/mol | Ccb | Emery and Benedict, 1911 | Corresponding ΔfHºliquid = -233.8 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
Quantity | Value | Units | Method | Reference | Comment |
S°liquid | 200.4 | J/mol*K | N/A | Kelley, 1929 | DH |
S°liquid | 200.0 | J/mol*K | N/A | Parks, Kelley, et al., 1929 | Extrapolation below 90 K, 54.0 J/mol*K. Revision of previous data.; DH |
S°liquid | 220.5 | J/mol*K | N/A | Parks and Kelley, 1928 | Extrapolation below 70 K, 60.04 J/mol*K.; DH |
S°liquid | 217.6 | J/mol*K | N/A | Parks and Kelley, 1925 | Extrapolation below 90 K, 71.63 J/mol*K.; DH |
Constant pressure heat capacity of liquid
Cp,liquid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
125.45 | 298.15 | Malhotra and Woolf, 1991 | T = 278 to 323 K. Cp(liq) = 1.337 + 2.7752x10-3(T/K) kJ/kg*K (278.15 to 323.15 K).; DH |
123.80 | 298.15 | Costas, Yao, et al., 1989 | DH |
126.6 | 298.15 | Petrov, Peshekhodov, et al., 1989 | T = 258.15, 278.15, 298.15, 318.15 K.; DH |
126.6 | 298.15 | Al'per, Peshekhodov, et al., 1986 | DH |
123.8 | 298.15 | Costas and Patterson, 1985 | T = 283.15, 298.15, 313.15 K.; DH |
123.8 | 298.15 | Costas and Patterson, 1985, 2 | DH |
125.9 | 298.15 | Saluja, Peacock, et al., 1979 | DH |
129.7 | 298. | Deshpande and Bhatagadde, 1971 | T = 298 to 318 K.; DH |
126.3 | 293. | Rastorguev and Ganiev, 1967 | T = 293 to 333 K.; DH |
125.56 | 298.2 | Low and Moelwyn-Hughes, 1962 | T = 253 to 308 K.; DH |
128.24 | 298. | Staveley, Tupman, et al., 1955 | T = 288 to 323 K.; DH |
128.4 | 302.4 | Phillip, 1939 | DH |
124.7 | 298. | Trew and Watkins, 1933 | DH |
124.7 | 298. | Trew, 1932 | DH |
124.68 | 296.99 | Kelley, 1929 | T = 16 to 298 K. Value is unsmoothed experimental datum.; DH |
124.3 | 260. | Mitsukuri and Hara, 1929 | T = 200 to 260 K.; DH |
123.8 | 298.4 | Parks and Kelley, 1928 | T = 70 to 289 K. Value is unsmoothed experimental datum.; DH |
124.7 | 289.4 | Parks and Kelley, 1925 | T = 70 to 290 K. Value is unsmoothed experimental datum.; DH |
125.9 | 293.2 | Williams and Daniels, 1925 | T = 20 to 40°C.; DH |
121.3 | 283. | Bramley, 1916 | Mean value, 0 to 20°C.; DH |
133.9 | 298. | von Reis, 1881 | T = 289 to 352 K.; DH |
Constant pressure heat capacity of solid
Cp,solid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
96. | 173. | Maass and Walbauer, 1925 | T = 93 to 173 K.; DH |
Phase change data
Go To: Top, Gas phase thermochemistry data, Condensed 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 |
---|---|---|---|---|---|
Tboil | 329.3 ± 0.3 | K | AVG | N/A | Average of 117 out of 129 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 178.7 ± 0.9 | K | AVG | N/A | Average of 11 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 178.5 | K | N/A | Wilhoit, Chao, et al., 1985 | Uncertainty assigned by TRC = 0.3 K; TRC |
Ttriple | 176.6 | K | N/A | Kelley, 1929, 2 | Crystal phase 1 phase; Uncertainty assigned by TRC = 0.15 K; deduced from appearance of a small maximum in heat capacity; TRC |
Ttriple | 177.6 | K | N/A | Parks and Kelley, 1928, 2 | Uncertainty assigned by TRC = 0.3 K; TRC |
Ttriple | 177.6 | K | N/A | Parks and Kelley, 1925, 2 | Uncertainty assigned by TRC = 0.2 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 508. ± 2. | K | AVG | N/A | Average of 19 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 48. ± 4. | bar | AVG | N/A | Average of 9 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 4.63 | mol/l | N/A | Campbell and Chatterjee, 1969 | Uncertainty assigned by TRC = 0.05 mol/l; TRC |
ρc | 4.03 | mol/l | N/A | Campbell and Chatterjee, 1968 | Uncertainty assigned by TRC = 0.026 mol/l; TRC |
ρc | 4.79 | mol/l | N/A | Kobe, Crawford, et al., 1955 | Uncertainty assigned by TRC = 0.17 mol/l; TRC |
ρc | 4.70 | mol/l | N/A | Rosenbaum, 1951 | Uncertainty assigned by TRC = 0.02 mol/l; TRC |
ρc | 4.34 | mol/l | N/A | Herz and Neukirch, 1923 | Uncertainty assigned by TRC = 0.03 mol/l; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 31.27 | kJ/mol | N/A | Majer and Svoboda, 1985 | |
ΔvapH° | 31.3 | kJ/mol | N/A | Ambrose, Ellender, et al., 1975 | AC |
ΔvapH° | 29.7 ± 0.004 | kJ/mol | V | Mathews, 1926 | ALS |
Reduced pressure boiling point
Tboil (K) | Pressure (bar) | Reference | Comment |
---|---|---|---|
329.3 | 0.027 | Buckingham and Donaghy, 1982 | BS |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
29.1 | 329.3 | N/A | Majer and Svoboda, 1985 | |
32.1 | 308. | N/A | Soni, Ramjugernath, et al., 2008 | Based on data from 298. to 318. K.; AC |
29.9 | 344. | A | Stephenson and Malanowski, 1987 | Based on data from 329. to 488. K.; AC |
32.9 | 228. | A | Stephenson and Malanowski, 1987 | Based on data from 178. to 243. K.; AC |
33.8 | 254. | A | Stephenson and Malanowski, 1987 | Based on data from 203. to 269. K.; AC |
30.6 | 338. | A | Stephenson and Malanowski, 1987 | Based on data from 323. to 379. K.; AC |
29.5 | 389. | A | Stephenson and Malanowski, 1987 | Based on data from 374. to 464. K.; AC |
29.7 | 472. | A | Stephenson and Malanowski, 1987 | Based on data from 457. to 508. K.; AC |
32.8 | 274. | A | Stephenson and Malanowski, 1987 | Based on data from 259. to 351. K. See also Ambrose, Sprake, et al., 1974 and Ambrose, Ellender, et al., 1975.; AC |
32.7 | 276. | A,EB | Stephenson and Malanowski, 1987 | Based on data from 261. to 328. K. See also Boublík and Aim, 1972.; AC |
31.9 | 300. | EB | Baliah and Gnanasekaran, 1986 | Based on data from 285. to 329. K.; AC |
26.1 | 373. | C | Dmitriev, Kachurina, et al., 1986 | AC |
21.7 | 423. | C | Dmitriev, Kachurina, et al., 1986 | AC |
15.3 | 473. | C | Dmitriev, Kachurina, et al., 1986 | AC |
9.2 | 498. | C | Dmitriev, Kachurina, et al., 1986 | AC |
31.8 | 319. | N/A | Castellari, Francesconi, et al., 1984 | Based on data from 305. to 333. K.; AC |
32.6 | 285. | N/A | Sokolov, Zhilina, et al., 1963 | Based on data from 278. to 293. K.; AC |
31.1 | 319. | N/A | Brown and Smith, 1957 | Based on data from 310. to 329. K.; AC |
29.09 | 338. | C | Pennington and Kobe, 1957 | ALS |
35. | 253. | MG | Felsing and Durban, 1926 | Based on data from 204. to 339. K.; AC |
32.1 | 293. | MG | Felsing and Durban, 1926 | Based on data from 204. to 339. K.; AC |
30.7 | 313. | MG | Felsing and Durban, 1926 | Based 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)
(kJ/mol)
Tr = reduced temperature (T / Tc)
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Temperature (K) | A (kJ/mol) | β | Tc (K) | Reference | Comment |
---|---|---|---|---|---|
300. to 345. | 46.95 | 0.2826 | 508.2 | Majer 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 | Comment |
---|---|---|---|---|---|
259.16 to 507.60 | 4.42448 | 1312.253 | -32.445 | Ambrose, Sprake, et al., 1974 | Coefficents calculated by NIST from author's data. |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
5.715 | 176.62 | Kelley, 1929 | DH |
5.72 | 176.6 | Domalski and Hearing, 1996 | AC |
5.690 | 177.6 | Parks and Kelley, 1928 | DH |
4.770 | 178.5 | Maass and Walbauer, 1925 | DH |
5.690 | 177.6 | Parks and Kelley, 1925 | DH |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
32.36 | 176.62 | Kelley, 1929 | DH |
32.0 | 177.6 | Parks and Kelley, 1928 | DH |
26.7 | 178.5 | Maass and Walbauer, 1925 | DH |
32.03 | 177.6 | Parks and Kelley, 1925 | DH |
Henry's Law data
Go To: Top, Gas phase thermochemistry data, Condensed 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) = k°H exp(d(ln(kH))/d(1/T) ((1/T) - 1/(298.15 K)))
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)
k°H (mol/(kg*bar)) | d(ln(kH))/d(1/T) (K) | Method | Reference | Comment |
---|---|---|---|---|
30. | 4600. | L | N/A | |
27. | 5300. | M | N/A | |
27. | M | N/A | ||
23. | Q | N/A | missing citation give several references for the Henry's law constants but don't assign them to specific species. | |
32. | 5800. | M | N/A | |
35. | 3800. | M | N/A | The data from Table 1 by missing citation was used to redo the regression analysis. The data for acetone in their Table 2 is wrong. |
3.0 | 3300. | X | N/A | |
26. | 4800. | M | N/A | |
30. | X | N/A | Value given here as quoted by missing citation. | |
25. | M | N/A | ||
25. | X | N/A | Value given here as quoted by missing citation. | |
25. | M | Buttery, Ling, et al., 1969 | ||
22. | 5000. | X | N/A | |
3.1 | R | N/A | ||
28. | M | N/A | ||
30. | R | N/A |
Gas phase ion energetics data
Go To: Top, Gas phase thermochemistry data, Condensed 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 ± 0.006 | eV | N/A | N/A | L |
Quantity | Value | Units | Method | Reference | Comment |
Proton affinity (review) | 812. | kJ/mol | N/A | Hunter and Lias, 1998 | HL |
Quantity | Value | Units | Method | Reference | Comment |
Gas basicity | 782.1 | kJ/mol | N/A | Hunter and Lias, 1998 | HL |
Electron affinity determinations
EA (eV) | Method | Reference | Comment |
---|---|---|---|
0.00152 | EFD | Desfrancois, Abdoul-Carime, et al., 1994 | EA: 1.5 meV. Dipole-bound state.; B |
Proton affinity at 298K
Proton affinity (kJ/mol) | Reference | Comment |
---|---|---|
>815.2 | Bouchoux, Buisson, et al., 2003 | MM |
>814.3 | Bouchoux, Buisson, et al., 2003 | MM |
>812.6 ± 0.2 | Bouchoux, Buisson, et al., 2003 | MM |
811.5 ± 3.4 | Bouchoux and Salpin, 1999 | T = 301K; Re-evaluated thermokinetic parametric fitting by the authors using reference base GBs and PAs from Hunter and Lias, 1998; MM |
811.5 ± 3.4 | Bouchoux and Salpin, 1999 | T = 298K; MM |
Gas basicity at 298K
Gas basicity (review) (kJ/mol) | Reference | Comment |
---|---|---|
784.7 | Bouchoux, Buisson, et al., 2003 | MM |
782.2 | Bouchoux, Buisson, et al., 2003 | MM |
782.0 ± 0.2 | Bouchoux, Buisson, et al., 2003 | MM |
782.1 ± 1.5 | Bouchoux and Salpin, 1999 | T = 301K; Re-evaluated thermokinetic parametric fitting by the authors using reference base GBs and PAs from Hunter and Lias, 1998; MM |
782.1 ± 1.5 | Bouchoux and Salpin, 1999 | T = 298K; MM |
Ionization energy determinations
Appearance energy determinations
De-protonation reactions
C3H5O- + =
By formula: C3H5O- + H+ = C3H6O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1543. ± 8.8 | kJ/mol | D-EA | Brinkman, Berger, et al., 1993 | gas phase; B |
ΔrH° | 1544. ± 8.8 | kJ/mol | G+TS | Bartmess, Scott, et al., 1979 | gas phase; value altered from reference due to change in acidity scale; B |
ΔrH° | 1546. ± 11. | kJ/mol | G+TS | Cumming and Kebarle, 1978 | gas phase; B |
ΔrH° | 1538. ± 7.5 | kJ/mol | EIAE | Muftakhov, Vasil'ev, et al., 1999 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1514. ± 8.4 | kJ/mol | IMRE | Bartmess, Scott, et al., 1979 | gas phase; value altered from reference due to change in acidity scale; B |
ΔrG° | 1516. ± 8.4 | kJ/mol | IMRE | Cumming and Kebarle, 1978 | gas phase; B |
References
Go To: Top, Gas phase thermochemistry data, Condensed 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]
Guinchant, 1918
Guinchant, M.J.,
Etude sur la fonction acide dans les derives metheniques et methiniques,
Ann. Chem., 1918, 10, 30-84. [all data]
Emery and Benedict, 1911
Emery, A.G.; Benedict, F.G.,
The heat of combustion of compounds of physiological importance,
Am. J. Physiol., 1911, 28, 301-307. [all data]
Kelley, 1929
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]
Parks, Kelley, et al., 1929
Parks, G.S.; Kelley, K.K.; Huffman, H.M.,
Thermal data on organic compounds. V. A revision of the entropies and free energies of nineteen organic compounds,
J. Am. Chem. Soc., 1929, 51, 1969-1973. [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, 734-750. [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, 2089-2097. [all data]
Malhotra and Woolf, 1991
Malhotra, R.; Woolf, L.A.,
Thermodynamic properties of propanone (acetone) at temperatures from 278 K to 323 K and pressures up to 400 Mpa,
J. Chem. Thermodynam., 1991, 23, 867-876. [all data]
Costas, Yao, et al., 1989
Costas, M.; Yao, Z.; Patterson, D.,
Complex formation and self-association in ternary mixtures, J. Chem. Soc.,
Faraday Trans., 1989, 1 85(8), 2211-2227. [all data]
Petrov, Peshekhodov, et al., 1989
Petrov, A.N.; Peshekhodov, P.B.; Al'per, G.A.,
Heat capacity of non-aqueous solutions of non-electrolyts with N,N-dimethylformamide as a base, Sbornik Nauch. Trud., Termodin. Rast. neelect., Ivanovo,
Inst. nevod. rast., 1989, Akad. [all data]
Al'per, Peshekhodov, et al., 1986
Al'per, G.A.; Peshekhodov, P.B.; Nikiforov, M.Yu.; Petrov, A.N.; Krestov, G.A.,
Specific heats and features of the intermolecular interactions in the system chloroform-acetone,
Zhur. Obshchei Khim., 1986, 56(8), 1688-1691. [all data]
Costas and Patterson, 1985
Costas, M.; Patterson, D.,
Heat capacities of water + organic-solvent mixtures, J. Chem. Soc.,
Faraday Trans. 1, 1985, 81, 2381-2398. [all data]
Costas and Patterson, 1985, 2
Costas, M.; Patterson, D.,
Self-association of alcohols in inert solvents, J. Chem. Soc.,
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Johnstone and Mellon, 1972
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Electron-impact ionization and appearance potentials,
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Brundle, Robin, et al., 1972
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Fragment ions from CH3CHO and (CH3)2CO by electron impact,
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Notes
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics data, References
- Symbols used in this document:
AE Appearance energy Cp,gas Constant pressure heat capacity of gas Cp,liquid Constant pressure heat capacity of liquid Cp,solid Constant pressure heat capacity of solid EA Electron affinity IE (evaluated) Recommended ionization energy Pc Critical pressure S°liquid Entropy of liquid at standard conditions Tboil Boiling point Tc Critical temperature Tfus Fusion (melting) point Ttriple Triple point temperature d(ln(kH))/d(1/T) Temperature dependence parameter for Henry's Law constant k°H Henry's Law constant at 298.15K ΔcH°gas Enthalpy of combustion of gas at standard conditions ΔcH°liquid Enthalpy of combustion of liquid at standard conditions ΔfH°gas Enthalpy of formation of gas at standard conditions ΔfH°liquid Enthalpy of formation of liquid at standard conditions ΔfusH Enthalpy of fusion ΔfusS Entropy of fusion ΔrG° Free energy of reaction at standard conditions ΔrH° Enthalpy of reaction at standard conditions ΔvapH Enthalpy of vaporization ΔvapH° Enthalpy of vaporization at standard conditions ρc Critical density - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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