Cyclohexanone
- Formula: C6H10O
- Molecular weight: 98.1430
- IUPAC Standard InChIKey: JHIVVAPYMSGYDF-UHFFFAOYSA-N
- CAS Registry Number: 108-94-1
- 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. - Other names: Anon; Anone; Hexanon; Hytrol O; Nadone; Pimelic ketone; Pimelin ketone; Sextone; Ketohexamethylene; Cicloesanone; Cyclohexanon; Cykloheksanon; NCI-C55005; Rcra waste number U057; UN 1915; Cyclohexyl ketone; NSC 5711
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Gas phase thermochemistry data
Go To: Top, Condensed phase thermochemistry data, Phase change 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 | -231.1 ± 0.88 | kJ/mol | Cm | Wiberg, Crocker, et al., 1991 | ALS |
ΔfH°gas | -225.7 | kJ/mol | Eqk | Kabo, Yursha, et al., 1988 | ALS |
ΔfH°gas | -227.7 ± 1.9 | kJ/mol | Ccb | Wolf, 1972 | ALS |
ΔfH°gas | -226.3 | kJ/mol | Ccb | Sellers and Sunner, 1962 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
S°gas | 335.53 | J/mol*K | N/A | Kabo G.J., 1988 | GT |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
121.06 | 298.15 | Kabo G.J., 1988 | Selected thermodynamic functions are in better agreement with experimental values of S(298.15 K) and Cp(T) than statistical values calculated by [ Thermodynamics Research Center, 1997, Andreevskii D.N., 1976]. Maximum discrepancies with functions given in [ Thermodynamics Research Center, 1997] amount to 2.5 and 5.0 J/mol*K for S(T) and Cp(T), respectively. Discrepancies with data [ Andreevskii D.N., 1976] reach 11 and 8 J/mol*K for S(T) and Cp(T), respectively.; GT |
121.89 | 300. | ||
161.88 | 400. | ||
196.39 | 500. | ||
225.24 | 600. | ||
249.27 | 700. | ||
269.47 | 800. | ||
286.51 | 900. | ||
301.06 | 1000. |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
155.20 | 385. | Shvaro O.V., 1987 | The experimental values of Cp(T) obtained by [ Vilcu R., 1975] seem to be not enough reliable in view of the comparison of experimental heat capacities of some alcohols and ketones measured by these authors (see [ Kabo G.J., 1995]).; GT |
161.07 | 400. | ||
168.98 | 420. | ||
175.81 | 440. | ||
183.65 | 460. | ||
190.18 | 480. |
Condensed phase thermochemistry data
Go To: Top, Gas phase thermochemistry data, Phase change 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
DH - Eugene S. Domalski and Elizabeth D. Hearing
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°liquid | -276.1 ± 0.84 | kJ/mol | Cm | Wiberg, Crocker, et al., 1991 | ALS |
ΔfH°liquid | -272.6 ± 1.8 | kJ/mol | Ccb | Wolf, 1972 | ALS |
ΔfH°liquid | -254. ± 2. | kJ/mol | Ccb | Rabinovoch, Tel'noy, et al., 1962 | ALS |
ΔfH°liquid | -271.4 | kJ/mol | Ccb | Sellers and Sunner, 1962 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -3517.6 ± 1.7 | kJ/mol | Ccb | Wolf, 1972 | Corresponding ΔfHºliquid = -272.58 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -3536. ± 2. | kJ/mol | Ccb | Rabinovoch, Tel'noy, et al., 1962 | Corresponding ΔfHºliquid = -254. kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -3518.9 ± 1.0 | kJ/mol | Ccb | Sellers and Sunner, 1962 | Corresponding ΔfHºliquid = -271.3 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -3499. ± 0.8 | kJ/mol | Ccb | Skuratov, Kozina, et al., 1957 | At 20C; Corresponding ΔfHºliquid = -291. kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
Quantity | Value | Units | Method | Reference | Comment |
S°liquid | 229.03 | J/mol*K | N/A | Nakamura, Suga, et al., 1980 | DH |
Constant pressure heat capacity of liquid
Cp,liquid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
177.20 | 300. | Nakamura, Suga, et al., 1980 | T = 13 to 300 K. Unsmoothed experimental datum for Cp at 296.40 K is 175.96 J/mol*K.; DH |
200.4 | 304.2 | Phillip, 1939 | DH |
177.8 | 290. | Herz and Bloch, 1924 | DH |
Phase change data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry 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
CAL - James S. Chickos, William E. Acree, Jr., Joel F. Liebman, Students of Chem 202 (Introduction to the Literature of Chemistry), University of Missouri -- St. Louis
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 428. ± 2. | K | AVG | N/A | Average of 21 out of 23 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 243. ± 10. | K | AVG | N/A | Average of 8 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 245.21 | K | N/A | Nakamura, Suga, et al., 1980, 2 | Crystal phase 1 phase; Uncertainty assigned by TRC = 0.01 K; TRC |
Ttriple | 242.4 | K | N/A | Wuerflinger and Kreutzenbeck, 1978 | Crystal phase 1 phase; Uncertainty assigned by TRC = 0.5 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 664.3 | K | N/A | Quadri and Kudchadker, 1991 | Uncertainty assigned by TRC = 3. K; TRC |
Tc | 653. | K | N/A | Ambrose and Ghiassee, 1987 | Uncertainty assigned by TRC = 3. K; TRC |
Tc | 629.15 | K | N/A | Glaser and Ruland, 1957 | Uncertainty assigned by TRC = 1.5 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 46.00 | bar | N/A | Quadri and Kudchadker, 1991 | Uncertainty assigned by TRC = 1.00 bar; TRC |
Pc | 40.00 | bar | N/A | Ambrose and Ghiassee, 1987 | Uncertainty assigned by TRC = 0.50 bar; TRC |
Pc | 38.5035 | bar | N/A | Glaser and Ruland, 1957 | Uncertainty assigned by TRC = 2.0265 bar; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 44. ± 4. | kJ/mol | AVG | N/A | Average of 7 values; Individual data points |
Reduced pressure boiling point
Tboil (K) | Pressure (bar) | Reference | Comment |
---|---|---|---|
320.2 | 0.020 | Weast and Grasselli, 1989 | BS |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
45.130 | 428.8 | N/A | Svoboda, Kubes, et al., 1992 | Value corrected to 298.15 K.; DH |
43.1 | 358. | EB | Teodorescu, Barhala, et al., 2006 | Based on data from 343. to 427. K.; AC |
44.0 | 333. | N/A | Aucejo, Monton, et al., 1993 | Based on data from 318. to 428. K.; AC |
44.4 ± 0.1 | 308. | C | Svoboda, Kubes, et al., 1992 | AC |
44.0 ± 0.1 | 313. | C | Svoboda, Kubes, et al., 1992 | AC |
43.4 ± 0.1 | 323. | C | Svoboda, Kubes, et al., 1992 | AC |
43.1 ± 0.1 | 328. | C | Svoboda, Kubes, et al., 1992 | AC |
42.2 ± 0.1 | 338. | C | Svoboda, Kubes, et al., 1992 | AC |
41.8 ± 0.1 | 343. | C | Svoboda, Kubes, et al., 1992 | AC |
41.4 ± 0.1 | 348. | C | Svoboda, Kubes, et al., 1992 | AC |
42.2 | 360. | EB | Ambrose and Ghiassee, 1987, 2 | Based on data from 345. to 458. K.; AC |
41.5 | 377. | A,EB | Stephenson and Malanowski, 1987 | Based on data from 362. to 439. K. See also Meyer and Hotz, 1973.; AC |
40.4 | 410. | N/A | Castellari, Francesconi, et al., 1984 | Based on data from 395. to 426. K.; AC |
40.3 | 286. | N/A | Radulescu and Alexa, 1938 | Based on data from 273. to 298. K.; AC |
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 |
---|---|---|---|---|
362.78 to 438.92 | 4.1033 ± 0.00099 | 1495.51 ± 0.67 | -63.598 ± 0.075 | Meyer and Hotz, 1973 |
Enthalpy of sublimation
ΔsubH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
49.3 | 254. | Nitta and Seki, 1948 | Based on data from 243. to 265. K.; AC |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
1.33 | 245.2 | Nakamura, Suga, et al., 1980 | AC |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
38.5 | 221. | Gonthier-Vassal and Szwarc, 1998 | CAL |
5.2 | 242.6 |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
39.22 | 220.8 | Nakamura, Suga, et al., 1980, 2 | CAL |
5.42 | 245.2 |
Enthalpy of phase transition
ΔHtrs (kJ/mol) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
8.6596 | 220.83 | crystaline, II | crystaline, I | Nakamura, Suga, et al., 1980 | DH |
1.3276 | 245.21 | crystaline, I | liquid | Nakamura, Suga, et al., 1980 | DH |
Entropy of phase transition
ΔStrs (J/mol*K) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
39.22 | 220.83 | crystaline, II | crystaline, I | Nakamura, Suga, et al., 1980 | DH |
5.414 | 245.21 | crystaline, I | liquid | Nakamura, Suga, et al., 1980 | DH |
References
Go To: Top, Gas phase thermochemistry data, Condensed 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.
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]
Kabo, Yursha, et al., 1988
Kabo, G.J.; Yursha, I.A.; Frenkel, M.L.; Poleshchuk, P.A.; Fedoseenko, V.I.; Ladutko, A.I.,
Thermodynamic properties of cyclohexanol and cyclohexanone,
J. Chem. Thermodyn., 1988, 20, 429-437. [all data]
Wolf, 1972
Wolf, G.,
Thermochemische Untersuchungen an cyclischen Ketonen,
Helv. Chim. Acta, 1972, 55, 1446-1459. [all data]
Sellers and Sunner, 1962
Sellers, P.; Sunner, S.,
Heats of combustion of cyclic ketones and alcohols,
Acta Chem. Scand., 1962, 16, 46-52. [all data]
Kabo G.J., 1988
Kabo G.J.,
Thermodynamic properties of cyclohexanol and cyclohexanone,
J. Chem. Thermodyn., 1988, 20, 429-437. [all data]
Thermodynamics Research Center, 1997
Thermodynamics Research Center,
Selected Values of Properties of Chemical Compounds., Thermodynamics Research Center, Texas A&M University, College Station, Texas, 1997. [all data]
Andreevskii D.N., 1976
Andreevskii D.N.,
Thermodynamic properties of C4-C6 cyclic ketones,
Zh. Prikl. Khim., 1976, 49, 1819-1823. [all data]
Shvaro O.V., 1987
Shvaro O.V.,
Thermodynamic properties of cyclopentanone and cyclohexanone,
Inzh.-Fiz. Zh., 1987, 52, 807-812. [all data]
Vilcu R., 1975
Vilcu R.,
Heat capacity of cyclohexanone and 4-methylcyclohexanone in the vapor phase,
Rev. Chim. (Bucharest), 1975, 26, 129-131. [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]
Rabinovoch, Tel'noy, et al., 1962
Rabinovoch, N.B.; Tel'noy, V.I.; Terman, L.M.; Kirillova, A.S.; Razuvaev, G.A.,
The heats of decomposition and formation of dicyclohexyl- and dimethylperoxidecarbonate,
Dokl. Akad. Nauk SSSR, 1962, 143, 133-136. [all data]
Skuratov, Kozina, et al., 1957
Skuratov, S.M.; Kozina, M.L.; Shteher, S.M.; Varushyenko, R.M.,
The heats of combustion of several purified compounds,
Thermochem. Bull. (Moscow State Univ.), March, 1957, 36-37. [all data]
Nakamura, Suga, et al., 1980
Nakamura, N.; Suga, H.; Seki, S.,
Calorimetric study on orientationally disordered crystals. Cyclohexene oxide and cyclohexanone,
Bull. Chem. Soc. Japan, 1980, 53(10), 2755-2761. [all data]
Phillip, 1939
Phillip, N.M.,
Adiabatic and isothermal compressibilities of liquids,
Proc. Indian Acad. Sci., 1939, A9, 109-120. [all data]
Herz and Bloch, 1924
Herz, W.; Bloch, W.,
Physikalisch-chemische Untersuchungen an Verbindungen der Cyklohexanreihe,
Z. Phys. Chem., 1924, 110, 23-39. [all data]
Nakamura, Suga, et al., 1980, 2
Nakamura, N.; Suga, H.; Seki, S.,
Calorimetric study on orientationally disordered crystals. Cyclohexene oxide and cyclohexanone.,
Bull. Chem. Soc. Japan, 1980, 53, 10, 2755, https://doi.org/10.1246/bcsj.53.2755
. [all data]
Wuerflinger and Kreutzenbeck, 1978
Wuerflinger, A.; Kreutzenbeck, J.,
J. Phys. Chem. Solids, 1978, 39, 193. [all data]
Quadri and Kudchadker, 1991
Quadri, S.K.; Kudchadker, A.P.,
Measurement of the critical temperatures and critical pressures of some thermally stable or mildly unstable esters, ketones, and ethers,
J. Chem. Thermodyn., 1991, 23, 129-34. [all data]
Ambrose and Ghiassee, 1987
Ambrose, D.; Ghiassee, N.B.,
Vapor Pressures and Critical Temperatures and Critical Pressures of C5 and C6 Cyclic Alcohols and Ketones,
J. Chem. Thermodyn., 1987, 19, 903. [all data]
Glaser and Ruland, 1957
Glaser, F.; Ruland, H.,
Untersuchungsen über dampfdruckkurven und kritische daten einiger technisch wichtiger organischer substanzen,
Chem. Ing. Techn., 1957, 29, 772. [all data]
Weast and Grasselli, 1989
CRC Handbook of Data on Organic Compounds, 2nd Editon, Weast,R.C and Grasselli, J.G., ed(s)., CRC Press, Inc., Boca Raton, FL, 1989, 1. [all data]
Svoboda, Kubes, et al., 1992
Svoboda, V.; Kubes, V.; Basarova, P.,
Enthalpies of vaporization and cohesive energies of hexan-2-one, 2-methylpentan-4-one, 2,2-dimethylbutan-3-one, 2,6-dimethylheptan-4-one and cyclohexanone,
J. Chem. Thermodynam., 1992, 24, 333-336. [all data]
Teodorescu, Barhala, et al., 2006
Teodorescu, Mariana; Barhala, Alexandru; Dragoescu, Dana,
Isothermal (vapour+liquid) equilibria for the binary (cyclopentanone or cyclohexanone with 1,1,2,2-tetrachloroethane) systems at temperatures of (343.15, 353.15, and 363.15)K,
The Journal of Chemical Thermodynamics, 2006, 38, 11, 1432-1437, https://doi.org/10.1016/j.jct.2006.01.010
. [all data]
Aucejo, Monton, et al., 1993
Aucejo, Antonio; Monton, Juan B.; Munoz, Rosa; Sanchotello, Margarita,
Isobaric vapor-liquid equilibrium data for the cyclohexanone + N-methylacetamide system,
J. Chem. Eng. Data, 1993, 38, 1, 160-162, https://doi.org/10.1021/je00009a039
. [all data]
Ambrose and Ghiassee, 1987, 2
Ambrose, D.; Ghiassee, N.B.,
Vapour pressures and critical temperatures and critical pressures of C5 and C6 cyclic alcohols and ketones,
The Journal of Chemical Thermodynamics, 1987, 19, 9, 903-909, https://doi.org/10.1016/0021-9614(87)90036-X
. [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]
Meyer and Hotz, 1973
Meyer, Edwin F.; Hotz, Roger D.,
High-precision vapor-pressure data for eight organic compounds,
J. Chem. Eng. Data, 1973, 18, 4, 359-362, https://doi.org/10.1021/je60059a008
. [all data]
Castellari, Francesconi, et al., 1984
Castellari, Carlo; Francesconi, Romolo; Comelli, Fabio,
Vapor-liquid equilibriums in binary systems containing 1,3-dioxolane at isobaric conditions. 5. Binary mixtures of 1,3-dioxolane with cyclohexanone and cyclohexanol,
J. Chem. Eng. Data, 1984, 29, 1, 90-93, https://doi.org/10.1021/je00035a029
. [all data]
Radulescu and Alexa, 1938
Radulescu, D.; Alexa, M.,
Bull. Chem. Soc. Romania, 1938, 20A, 89. [all data]
Nitta and Seki, 1948
Nitta, I.; Seki, S.,
J. Chem. Soc. Jpn. Pure Chem. Sect., 1948, 69, 141. [all data]
Gonthier-Vassal and Szwarc, 1998
Gonthier-Vassal, A.; Szwarc, H.,
Thermochim. Acta, 1998, 141. [all data]
Notes
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, References
- Symbols used in this document:
Cp,gas Constant pressure heat capacity of gas Cp,liquid Constant pressure heat capacity of liquid Pc Critical pressure S°gas Entropy of gas at standard conditions S°liquid Entropy of liquid at standard conditions Tboil Boiling point Tc Critical temperature Tfus Fusion (melting) point Ttriple Triple point temperature ΔHtrs Enthalpy of phase transition ΔStrs Entropy of phase transition 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 ΔsubH Enthalpy of sublimation ΔvapH Enthalpy of vaporization ΔvapH° Enthalpy of vaporization at standard conditions - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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