Cyclohexanol
- Formula: C6H12O
- Molecular weight: 100.1589
- IUPAC Standard InChIKey: HPXRVTGHNJAIIH-UHFFFAOYSA-N
- CAS Registry Number: 108-93-0
- 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: Cyclohexyl alcohol; Adronal; Adronol; Anol; Hexahydrophenol; Hexalin; Hydroxycyclohexane; Naxol; Phenol, hexahydro-; 1-Cyclohexanol; Cyclohexane, hydroxy-; Hydralin; Cicloesanolo; Cykloheksanol; Hydrophenol; NSC 403656
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Gas phase thermochemistry data
Go To: Top, Condensed phase thermochemistry data, Phase change data, Reaction 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:
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
DRB - Donald R. Burgess, Jr.
GT - Glushko Thermocenter, Russian Academy of Sciences, Moscow
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°gas | -290. ± 8. | kJ/mol | AVG | N/A | Average of 6 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
S°gas | 353.83 | J/mol*K | N/A | Kabo G.J., 1988 | Other entropy value at 298.15 K obtained from calorimetric data is 327.69 J/mol*K [ Stull D.R., 1969].; GT |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
132.70 | 298.15 | Kabo G.J., 1988 | Statistically calculated S(T) and Cp(T) values given in [ Thermodynamics Research Center, 1997] are 1-10 and 5-10 J/mol*K, respectively, lower than those of [ Kabo G.J., 1988].; GT |
133.53 | 300. | ||
176.60 | 400. | ||
216.42 | 500. | ||
250.18 | 600. | ||
278.37 | 700. | ||
301.73 | 800. | ||
320.77 | 900. | ||
337.32 | 1000. |
Condensed phase thermochemistry data
Go To: Top, Gas phase thermochemistry data, Phase change data, Reaction 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:
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 | -352.0 ± 0.67 | kJ/mol | Cac | Wiberg, Wasserman, et al., 1985 | Trifluoroacetolysis; ALS |
ΔfH°liquid | -350. ± 2. | kJ/mol | Ccb | Rabinovoch, Tel'noy, et al., 1962 | ALS |
ΔfH°liquid | -347.4 ± 2.2 | kJ/mol | Ccb | Sellers and Sunner, 1962 | Reanalyzed by Cox and Pilcher, 1970, Original value = -348.2 kJ/mol; ALS |
ΔfH°liquid | -349.2 ± 0.2 | kJ/mol | Ccb | Parks, Mosley, et al., 1950 | ALS |
ΔfH°liquid | -359.2 | kJ/mol | Ccb | Kelley, 1929 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -3730. ± 20. | kJ/mol | AVG | N/A | Average of 6 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
S°liquid | 203.87 | J/mol*K | N/A | Adachi, Suga, et al., 1968 | DH |
S°liquid | 199.6 | J/mol*K | N/A | Kelley, 1929 | Average of values derived from measurements on both low and high temperature crystal forms down to 13 K, plus entropy of transition and fusion. Debye extrapolation below 13.5 K.; DH |
Constant pressure heat capacity of liquid
Cp,liquid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
214.06 | 298.15 | Mayer, Rachwalska, et al., 1990 | T = 170 to 320 K. Cp(liq) = -2223.2606 + 22.0059595T - 0.0691686793T2 + 0.0000763592T3 J/mol*K (298 to 320 K). Cp value caluculated from equation.; DH |
209.99 | 298.15 | Caceres-Alonso, Costas, et al., 1988 | DH |
220.1 | 298. | Conti, Gianni, et al., 1976 | DH |
212. | 297.95 | Petit and TerMinassian, 1974 | T = 297 to 428 K. Value is unsmoothed experimental datum.; DH |
213.59 | 300. | Adachi, Suga, et al., 1968 | T = 14 to 320 K.; DH |
202.5 | 305.1 | Phillip, 1939 | DH |
209.03 | 298.15 | Kelley, 1929 | T = 13 to 300 K. Value is unsmoothed experimental datum.; DH |
174.9 | 290. | Herz and Bloch, 1924 | DH |
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
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
DRB - Donald R. Burgess, Jr.
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
DH - Eugene S. Domalski and Elizabeth D. Hearing
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 433. ± 3. | K | AVG | N/A | Average of 20 out of 21 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 296. ± 5. | K | AVG | N/A | Average of 9 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 299.09 | K | N/A | Adachi, Suga, et al., 1968, 2 | Crystal phase 1 phase; Uncertainty assigned by TRC = 0.02 K; TRC |
Ttriple | 297.0 | K | N/A | Kelley, 1929, 2 | Crystal phase 1 phase; Uncertainty assigned by TRC = 0.2 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 645. ± 20. | K | AVG | N/A | Average of 6 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 40.80 | bar | N/A | Steele, Chirico, et al., 1997 | Uncertainty assigned by TRC = 1.50 bar; derived from fit of obs. vapor pressure; TRC |
Pc | 44.01 | bar | N/A | Wilson, Wilson, et al., 1996 | Uncertainty assigned by TRC = 0.25 bar; TRC |
Pc | 42.6 ± 0.5 | bar | N/A | Gude and Teja, 1995 | |
Pc | 42.60 | bar | N/A | Ambrose and Ghiassee, 1987 | Uncertainty assigned by TRC = 0.50 bar; TRC |
Pc | 37.4902 | bar | N/A | Glaser and Ruland, 1957 | Uncertainty assigned by TRC = 1.5199 bar; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 3.00 | mol/l | N/A | Steele, Chirico, et al., 1997 | Uncertainty assigned by TRC = 0.10 mol/l; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 62. ± 1. | kJ/mol | AVG | N/A | Average of 10 out of 11 values; Individual data points |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
60.1 | 337. | N/A | Steyer and Sundmacher, 2004 | Based on data from 322. to 433. K.; AC |
49.8 | 405. | N/A | Swiatek and Malanowski, 2002 | Based on data from 390. to 430. K.; AC |
61.2 ± 0.6 | 308. | GS | Verevkin, 1998 | Based on data from 288. to 328. K.; AC |
55.0 | 365. | EB | Ambrose and Ghiassee, 1987, 2 | Based on data from 350. to 456. K.; AC |
59.9 | 333. | A | Stephenson and Malanowski, 1987 | Based on data from 318. to 434. K.; AC |
62.7 | 315. | A | Stephenson and Malanowski, 1987 | Based on data from 300. to 434. K.; AC |
49.3 | 418. | N/A | Castellari, Francesconi, et al., 1984 | Based on data from 404. to 432. K.; AC |
58.4 | 318. | N/A | Sipowska and Wieczorek, 1984 | Based on data from 303. to 373. K.; AC |
60.4 | 309. | N/A | Cabani, Conti, et al., 1975 | Based on data from 299. to 319. K.; AC |
52.6 | 382. | N/A | Novák, Matous, et al., 1960 | Based on data from 367. to 433. K. See also Novák, Matous, et al., 1960, 2.; AC |
54.8 | 322. | N/A | Thomson, 1946 | Based on data from 307. to 422. K.; AC |
45.44 | 431.7 | V | Mathews and Fehlandt, 1931 | ALS |
Antoine Equation Parameters
log10(P) = A − (B / (T + C))
P = vapor pressure (bar)
T = temperature (K)
View plot Requires a JavaScript / HTML 5 canvas capable browser.
Temperature (K) | A | B | C | Reference | Comment |
---|---|---|---|---|---|
366.88 to 433.9 | 3.08077 | 777.363 | -182.037 | Novak, Matous, et al., 1960 | Coefficents calculated by NIST from author's data. |
Enthalpy of sublimation
ΔsubH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
60.7 | 285. | A | Stephenson and Malanowski, 1987 | Based on data from 272. to 298. K. See also Nitta and Seki, 1948.; AC |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
1.73 | 298.2 | DSC | Singh and Murthy, 2009 | AC |
1.7 | 297. | N/A | Pingel, Poser, et al., 1984 | See also Adachi, Suga, et al., 1968 and Domalski and Hearing, 1996.; AC |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
31.14 | 263.5 | Domalski and Hearing, 1996 | CAL |
5.72 | 297. |
Enthalpy of phase transition
ΔHtrs (kJ/mol) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
0.3784 | 220.9 | crystaline, III | crystaline, II | Mayer, Rachwalska, et al., 1990 | DH |
8.620 | 244.5 | crystaline, III | crystaline, I | Mayer, Rachwalska, et al., 1990 | DH |
8.662 | 264.86 | crystaline, II | crystaline, I | Mayer, Rachwalska, et al., 1990 | DH |
1.806 | 297.92 | crystaline, I | liquid | Mayer, Rachwalska, et al., 1990 | DH |
8.640 | 244.8 | crystaline, III | crystaline, I | Adachi, Suga, et al., 1968 | DH |
8.827 | 265.50 | crystaline, II | crystaline, I | Adachi, Suga, et al., 1968 | DH |
1.783 | 299.09 | crystaline, I | liquid | Adachi, Suga, et al., 1968 | DH |
8.205 | 263.5 | crystaline, II | crystaline, I | Kelley, 1929 | Excess enthalpy over extrapolated heat capacity curves.; DH |
1.699 | 297.0 | crystaline, I | liquid | Kelley, 1929 | Tm is 23.87°C from 16RIC/SHI.; DH |
Entropy of phase transition
ΔStrs (J/mol*K) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
1.713 | 220.9 | crystaline, III | crystaline, II | Mayer, Rachwalska, et al., 1990 | DH |
35.3 | 244.5 | crystaline, III | crystaline, I | Mayer, Rachwalska, et al., 1990 | DH |
32.70 | 264.86 | crystaline, II | crystaline, I | Mayer, Rachwalska, et al., 1990 | DH |
6.06 | 297.92 | crystaline, I | liquid | Mayer, Rachwalska, et al., 1990 | DH |
35.29 | 244.8 | crystaline, III | crystaline, I | Adachi, Suga, et al., 1968 | DH |
33.25 | 265.50 | crystaline, II | crystaline, I | Adachi, Suga, et al., 1968 | DH |
5.96 | 299.09 | crystaline, I | liquid | Adachi, Suga, et al., 1968 | DH |
31.14 | 263.5 | crystaline, II | crystaline, I | Kelley, 1929 | Excess; DH |
5.72 | 297.0 | crystaline, I | liquid | Kelley, 1929 | Tm; DH |
Reaction thermochemistry data
Go To: Top, Gas phase thermochemistry data, 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 by: Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
Note: Please consider using the reaction search for this species. This page allows searching of all reactions involving this species. A general reaction search form is also available. Future versions of this site may rely on reaction search pages in place of the enumerated reaction displays seen below.
Individual Reactions
By formula: C6H10O + H2 = C6H12O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -75.86 ± 0.50 | kJ/mol | Cm | Wiberg, Crocker, et al., 1991 | liquid phase |
ΔrH° | -63.51 ± 0.63 | kJ/mol | Chyd | Conn, Kistiakowsky, et al., 1939 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -64.5 ± 0.3 kJ/mol; At 355 K |
By formula: C6H12O + C4F6O3 = C8H11F3O2 + C2HF3O2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -90.06 ± 0.15 | kJ/mol | Cac | Wiberg, Wasserman, et al., 1985 | liquid phase; Trifluoroacetolysis |
By formula: C6H12O = C6H10O + H2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 63.4 ± 2.3 | kJ/mol | Eqk | Kabo, Yursha, et al., 1988 | gas phase; Dehydrogenation |
By formula: C6H12O + C3H6O = C6H10O + C3H8O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 9.9 ± 1.9 | kJ/mol | Eqk | Fedoseenko, Yursha, et al., 1983 | gas phase; At 503 K |
By formula: C6H12O = C6H12 + H2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 63.4 ± 2.3 | kJ/mol | Eqk | Fedoseenko, Yursha, et al., 1983 | gas phase; At 502 K |
By formula: C6H10O + C5H10O = C6H12O + C5H8O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -11.6 ± 1.7 | kJ/mol | Eqk | Fedoseenko, Yursha, et al., 1984 | gas phase |
By formula: C6H10O + C3H8O = C6H12O + C3H6O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -9.9 ± 1.9 | kJ/mol | Eqk | Kabo, Yursha, et al., 1988 | gas phase |
References
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Kabo G.J., 1988
Kabo G.J.,
Thermodynamic properties of cyclohexanol and cyclohexanone,
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Stull D.R., 1969
Stull D.R., Jr.,
The Chemical Thermodynamics of Organic Compounds. Wiley, New York, 1969. [all data]
Thermodynamics Research Center, 1997
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Selected Values of Properties of Chemical Compounds., Thermodynamics Research Center, Texas A&M University, College Station, Texas, 1997. [all data]
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Wiberg, K.B.; Wasserman, D.J.; Martin, E.J.; Murcko, M.A.,
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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,
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Sellers and Sunner, 1962
Sellers, P.; Sunner, S.,
Heats of combustion of cyclic ketones and alcohols,
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Cox and Pilcher, 1970
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Cyclohexanol and the third law of thermodynamics,
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Phase changes in crystalline and glassy-crystalline cyclohexanol,
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On the polymorphism of solid cyclohexanol by adiabatic calorimetry and far infrared methods,
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Phase Changes in Crystalline and Glassy-Crystalline Cyclohexanol,
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Vapor-Liquid Equilibrium in m -Xylene + Cyclohexanol at 19.99 and 94.93 kPa,
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Gleichgewicht flüssigkeit-dampf XXIV. Gleichgewicht flüssigkeit-dampf im system cyclohexylamin-cyclohexanol-anilin,
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Dampfdruck des cyclohexanols und des cyclohexylamins,
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The heats of vaporization of some organic compounds,
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Dampfdruck des Cyclohexanols und des Cyclohexylamins,
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Dielectric and calorimetric investigation of an unusual two-component plastic crystal: cyclohexanol-neopentylglycol,
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Wiberg, Crocker, et al., 1991
Wiberg, K.B.; Crocker, L.S.; Morgan, K.M.,
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Conn, Kistiakowsky, et al., 1939
Conn, J.B.; Kistiakowsky, G.B.; Smith, E.A.,
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Kabo, Yursha, et al., 1988
Kabo, G.J.; Yursha, I.A.; Frenkel, M.L.; Poleshchuk, P.A.; Fedoseenko, V.I.; Ladutko, A.I.,
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Fedoseenko, Yursha, et al., 1983
Fedoseenko, V.I.; Yursha, I.A.; Kabo, G.Ya.,
Equilibrium and thermodynamics of cyclohexanol dehydrogenation reactions,
Dokl. Akad. Nauk BSSR, 1983, 27, 926-929. [all data]
Fedoseenko, Yursha, et al., 1984
Fedoseenko, V.I.; Yursha, I.A.; Kabo, G.Ya.,
Equilibrium of cyclopentanol dehydrogenation and hydrogen disproportionation in the cyclopentanol-cyclohexanone system,
Dokl. Akad. Nauk BSSR, 1984, 28, 1109-1112. [all data]
Notes
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- 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 ΔrH° Enthalpy of reaction at standard conditions ΔsubH Enthalpy of sublimation 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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