Cyclohexane
- Formula: C6H12
- Molecular weight: 84.1595
- IUPAC Standard InChIKey: XDTMQSROBMDMFD-UHFFFAOYSA-N
- CAS Registry Number: 110-82-7
- 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: Benzene, hexahydro-; Hexahydrobenzene; Hexamethylene; Hexanaphthene; Cicloesano; Cykloheksan; Rcra waste number U056; UN 1145; NSC 406835
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- Other data available:
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Phase change data
Go To: Top, 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
DRB - Donald R. Burgess, Jr.
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 | 353.9 ± 0.2 | K | AVG | N/A | Average of 93 out of 116 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 279.6 ± 0.3 | K | AVG | N/A | Average of 38 out of 47 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 279.7 ± 0.4 | K | AVG | N/A | Average of 8 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 554. ± 1. | K | AVG | N/A | Average of 18 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 40.7 ± 0.5 | bar | AVG | N/A | Average of 8 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Vc | 0.308 | l/mol | N/A | Daubert, 1996 | |
Vc | 0.309 | l/mol | N/A | Young, 1972 | Uncertainty assigned by TRC = 0.003 l/mol; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 3.24 ± 0.03 | mol/l | N/A | Daubert, 1996 | |
ρc | 3.26 | mol/l | N/A | Teja and Anselme, 1990 | Uncertainty assigned by TRC = 0.07 mol/l; TRC |
ρc | 3.230 | mol/l | N/A | Simon, 1957 | Uncertainty assigned by TRC = 0.04 mol/l; TRC |
ρc | 3.250 | mol/l | N/A | Young, 1910 | Uncertainty assigned by TRC = 0.02 mol/l; TRC |
ρc | 3.247 | mol/l | N/A | Young and Fortey, 1899 | Uncertainty assigned by TRC = 0.06 mol/l; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 33.1 ± 0.4 | kJ/mol | AVG | N/A | Average of 19 out of 21 values; Individual data points |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
29.97 | 353.9 | N/A | Majer and Svoboda, 1985 | |
33.334 | 298.15 | N/A | Aston, Szasa, et al., 1943 | P = 13.18 kPa; DH |
33.1 | 315. | EB | Gierycz, Kosowski, et al., 2009 | Based on data from 296. to 353. K.; AC |
32.7 | 315. | N/A | Lubomska, Banas, et al., 2002 | Based on data from 300. to 345. K.; AC |
31.9 | 324. | EB | Diogo, Santos, et al., 1995 | Based on data from 313. to 336. K.; AC |
32.2 | 375. | N/A | Lee and Holder, 1993 | Based on data from 360. to 470. K.; AC |
32.3 | 314. | C | Dong, Lin, et al., 1988 | AC |
31.1 | 332. | C | Dong, Lin, et al., 1988 | AC |
30.3 | 345. | C | Dong, Lin, et al., 1988 | AC |
30.0 | 355. | C | Dong, Lin, et al., 1988 | AC |
30.9 | 368. | A | Stephenson and Malanowski, 1987 | Based on data from 353. to 414. K.; AC |
29.6 | 427. | A | Stephenson and Malanowski, 1987 | Based on data from 412. to 491. K.; AC |
29.6 | 504. | A | Stephenson and Malanowski, 1987 | Based on data from 489. to 553. K.; AC |
32.9 | 308. | A,MM | Stephenson and Malanowski, 1987 | Based on data from 293. to 355. K. See also Willingham, Taylor, et al., 1945.; AC |
32.3 ± 0.1 | 313. | C | Majer, Svoboda, et al., 1979 | AC |
31.2 ± 0.1 | 333. | C | Majer, Svoboda, et al., 1979 | AC |
31.0 ± 0.1 | 338. | C | Majer, Svoboda, et al., 1979 | AC |
30.4 ± 0.1 | 348. | C | Majer, Svoboda, et al., 1979 | AC |
30.1 ± 0.1 | 353. | C | Majer, Svoboda, et al., 1979 | AC |
32.2 ± 0.1 | 313. | C | Svoboda, Veselý, et al., 1973 | AC |
31.9 ± 0.1 | 323. | C | Svoboda, Veselý, et al., 1973 | AC |
31.1 ± 0.1 | 333. | C | Svoboda, Veselý, et al., 1973 | AC |
30.6 ± 0.1 | 343. | C | Svoboda, Veselý, et al., 1973 | AC |
30.1 ± 0.1 | 354. | C | Svoboda, Veselý, et al., 1973 | AC |
32.5 | 318. | N/A | Gaw and Swinton, 1968 | Based on data from 303. to 343. K.; AC |
32.9 | 313. | N/A | Cruickshank and Cutler, 1967 | Based on data from 298. to 348. K.; AC |
32.8 | 331. | N/A | Marinichev and Susarev, 1965 | Based on data from 316. to 354. K.; AC |
31.4 ± 0.1 | 324. | C | McCullough, Person, et al., 1951 | AC |
30.4 ± 0.1 | 346. | C | McCullough, Person, et al., 1951 | AC |
30.1 | 354. | N/A | Spitzer and Pitzer, 1946 | 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)
View plot Requires a JavaScript / HTML 5 canvas capable browser.
Temperature (K) | 292. to 422. |
---|---|
A (kJ/mol) | 43.32 |
α | -0.1437 |
β | 0.4512 |
Tc (K) | 553.4 |
Reference | Majer and Svoboda, 1985 |
Entropy of vaporization
ΔvapS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
111.80 | 298.15 | Aston, Szasa, et al., 1943 | P; DH |
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 |
---|---|---|---|---|---|
323. to 523. | 4.13983 | 1316.554 | -35.581 | Kerns, Anthony, et al., 1974 | Coefficents calculated by NIST from author's data. |
303. to 343. | 3.9920 | 1216.93 | -48.621 | Gaw and Swinton, 1968, 2 | Coefficents calculated by NIST from author's data. |
315.70 to 353.90 | 3.17125 | 780.637 | -107.29 | Marinichev and Susarev, 1965, 2 | Coefficents calculated by NIST from author's data. |
293.06 to 354.73 | 3.96988 | 1203.526 | -50.287 | Williamham, Taylor, et al., 1945 |
Enthalpy of sublimation
ΔsubH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
27.6 | 265. | A | Stephenson and Malanowski, 1987 | Based on data from 223. to 280. K.; AC |
46.6 | 186. | B | Bondi, 1963 | AC |
37.2 | 273. | N/A | Jones, 1960 | Based on data from 268. to 278. K.; AC |
37.7 | 248. | A | Stull, 1947 | Based on data from 228. to 268. K.; AC |
36.5 | 274. | A | Rotinjanz and Nagornow, 1934 | Based on data from 269. to 279. K.; AC |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
2.68 | 279.8 | Domalski and Hearing, 1996 | AC |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
36.2 | 186.1 | Domalski and Hearing, 1996 | CAL |
9.57 | 279.8 |
Enthalpy of phase transition
ΔHtrs (kJ/mol) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
6.686 | 186.09 | crystaline, II | crystaline, I | Aston, Szasa, et al., 1943 | DH |
2.628 | 279.84 | crystaline, I | liquid | Aston, Szasa, et al., 1943 | DH |
6.7396 | 186.1 | crystaline, II | crystaline, I | Ruehrwein and Huffman, 1943 | DH |
2.6769 | 279.82 | crystaline, I | liquid | Ruehrwein and Huffman, 1943 | DH |
6.820 | 186.4 | crystaline, II | crystaline, I | Ziegler and Andrews, 1942 | DH |
2.728 | 279.4 | crystaline, I | liquid | Ziegler and Andrews, 1942 | DH |
6.234 | 185.9 | crystaline, II | crystaline, I | Parks, Huffman, et al., 1930 | DH |
2.423 | 279.3 | crystaline, I | liquid | Parks, Huffman, et al., 1930 | DH |
Entropy of phase transition
ΔStrs (J/mol*K) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
35.93 | 186.09 | crystaline, II | crystaline, I | Aston, Szasa, et al., 1943 | DH |
9.39 | 279.84 | crystaline, I | liquid | Aston, Szasa, et al., 1943 | DH |
36.21 | 186.1 | crystaline, II | crystaline, I | Ruehrwein and Huffman, 1943 | DH |
9.57 | 279.82 | crystaline, I | liquid | Ruehrwein and Huffman, 1943 | DH |
36.59 | 186.4 | crystaline, II | crystaline, I | Ziegler and Andrews, 1942 | DH |
9.76 | 279.4 | crystaline, I | liquid | Ziegler and Andrews, 1942 | DH |
33.53 | 185.9 | crystaline, II | crystaline, I | Parks, Huffman, et al., 1930 | DH |
8.68 | 279.3 | crystaline, I | liquid | Parks, Huffman, et al., 1930 | DH |
References
Go To: Top, Phase change data, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Daubert, 1996
Daubert, T.E.,
Vapor-Liquid Critical Properties of Elements and Compounds. 5. Branched Alkanes and Cycloalkanes,
J. Chem. Eng. Data, 1996, 41, 365-372. [all data]
Young, 1972
Young, C.L.,
Gas-liquid critical properties of the cycloalkanes and their mixtures,
Aust. J. Chem., 1972, 25, 1625-30. [all data]
Teja and Anselme, 1990
Teja, A.S.; Anselme, M.J.,
The critical properties of thermally stable and unstable fluids. II. 1986 results,
AIChE Symp. Ser., 1990, 86, 279, 122-7. [all data]
Simon, 1957
Simon, M.,
Methods and Apparatus Used at the Bureau of Physicochemical Standards XV. Critical Constants and Straight-Line Diameters of Ten Hydrocarbons,
Bull. Soc. Chim. Belg., 1957, 66, 375-81. [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 and Fortey, 1899
Young, S.; Fortey, E.C.,
The Vapour Pressures, Specific Volumes and Critical Constants of Hexamethylene.,
J. Chem. Soc., Trans., 1899, 75, 873. [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]
Aston, Szasa, et al., 1943
Aston, J.G.; Szasa, G.J.; Fink, H.L.,
The heat capacity and entropy, heats of transition, fusion and vaporization and the vapor pressures of cyclohexane. The vibrational frequencies of alicyclic ring systems,
J. Am. Chem. Soc., 1943, 65, 1135-1139. [all data]
Gierycz, Kosowski, et al., 2009
Gierycz, Pawel; Kosowski, Andrzej; Swietlik, Ryszard,
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols,
J. Chem. Eng. Data, 2009, 54, 11, 2996-3001, https://doi.org/10.1021/je900050z
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Lubomska, Banas, et al., 2002
Lubomska, Monika; Banas, Agnieszka; Malanowski, Stanislaw K.,
Vapor-Liquid Equilibrium in Binary Systems Formed by Allyl Alcohol with Benzene and with Cyclohexane,
J. Chem. Eng. Data, 2002, 47, 6, 1466-1471, https://doi.org/10.1021/je025540l
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Diogo, Santos, et al., 1995
Diogo, Hermínio P.; Santos, Rui C.; Nunes, Paulo M.; Minas da Piedade, Manuel E.,
Ebulliometric apparatus for the measurement of enthalpies of vaporization,
Thermochimica Acta, 1995, 249, 113-120, https://doi.org/10.1016/0040-6031(95)90678-9
. [all data]
Lee and Holder, 1993
Lee, Chang Ha; Holder, Gerald D.,
Vapor-liquid equilibria in the systems toluene/naphthalene and cyclohexane/naphthalene,
J. Chem. Eng. Data, 1993, 38, 2, 320-323, https://doi.org/10.1021/je00010a034
. [all data]
Dong, Lin, et al., 1988
Dong, Jin-Quan; Lin, Rui-Sen; Yen, Wen-Hsing,
Heats of vaporization and gaseous molar heat capacities of ethanol and the binary mixture of ethanol and benzene,
Can. J. Chem., 1988, 66, 4, 783-790, https://doi.org/10.1139/v88-136
. [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
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Willingham, Taylor, et al., 1945
Willingham, C.B.; Taylor, W.J.; Pignocco, J.M.; Rossini, F.D.,
Vapor pressures and boiling points of some paraffin, alkylcyclopentane, alkylcyclohexane, and alkylbenzene hydrocarbons,
J. RES. NATL. BUR. STAN., 1945, 35, 3, 219-17, https://doi.org/10.6028/jres.035.009
. [all data]
Majer, Svoboda, et al., 1979
Majer, Vladimír; Svoboda, Václav; Hála, Slavoj; Pick, Jirí,
Temperature dependence of heats of vaporization of saturated hydrocarbons C5-C8; Experimental data and an estimation method,
Collect. Czech. Chem. Commun., 1979, 44, 3, 637-651, https://doi.org/10.1135/cccc19790637
. [all data]
Svoboda, Veselý, et al., 1973
Svoboda, V.; Veselý, F.; Holub, R.; Pick, J.,
Enthalpy data of liquids. II. The dependence of heats of vaporization of methanol, propanol, butanol, cyclohexane, cyclohexene, and benzene on temperature,
Collect. Czech. Chem. Commun., 1973, 38, 12, 3539-3543, https://doi.org/10.1135/cccc19733539
. [all data]
Gaw and Swinton, 1968
Gaw, W.J.; Swinton, F.L.,
Thermodynamic properties of binary systems containing hexafluorobenzene. Part 3.?Excess Gibbs free energy of the system hexafluorobenzene + cyclohexane,
Trans. Faraday Soc., 1968, 64, 637, https://doi.org/10.1039/tf9686400637
. [all data]
Cruickshank and Cutler, 1967
Cruickshank, Austin J.B.; Cutler, A.J.B.,
Vapor pressure of cyclohexane, 25 to 75.degree.,
J. Chem. Eng. Data, 1967, 12, 3, 326-329, https://doi.org/10.1021/je60034a010
. [all data]
Marinichev and Susarev, 1965
Marinichev, A.N.; Susarev, M.P.,
Zh. Prikl. Khim. (S.-Peterburg), 1965, 38, 378. [all data]
McCullough, Person, et al., 1951
McCullough, J.P.; Person, W.B.; Spitzer, Ralph,
The Heats of Vaporization and Vapor Heat Capacities of Some Dimethylcyclohexanes 1,
J. Am. Chem. Soc., 1951, 73, 9, 4069-4071, https://doi.org/10.1021/ja01153a003
. [all data]
Spitzer and Pitzer, 1946
Spitzer, Ralph; Pitzer, Kenneth S.,
The Heat Capacity of Gaseous Cyclopentane, Cyclohexane and Methylcyclohexane,
J. Am. Chem. Soc., 1946, 68, 12, 2537-2538, https://doi.org/10.1021/ja01216a032
. [all data]
Kerns, Anthony, et al., 1974
Kerns, W.J.; Anthony, R.G.; Eubank, P.T.,
Volumetric Properties of Cyclohexane Vapor,
AIChE Symp. Ser., 1974, 70, 140, 14-21. [all data]
Gaw and Swinton, 1968, 2
Gaw, W.J.; Swinton, F.L.,
Thermodynamic Properties of Binary Systems Containing Hexafluorobenzene. Part 3. Excess Gibbs Free Energy of the System Hexafluorobenzene + Cyclohexane,
Trans. Faraday Soc., 1968, 64, 637-647, https://doi.org/10.1039/tf9686400637
. [all data]
Marinichev and Susarev, 1965, 2
Marinichev, A.N.; Susarev, M.P.,
Study of a Liquid-Vapor Equilibrium in the Systems of Acetone/Methanol and Acetone/Cyclohexane at Temperatures 35, 45, 55 ºC and Pressure 760 Torr,
Zh. Prikl. Khim. (Moscow), 1965, 38, 378-383. [all data]
Williamham, Taylor, et al., 1945
Williamham, C.B.; Taylor, W.J.; Pignocco, J.M.; Rossini, F.D.,
Vapor Pressures and Boiling Points of Some Paraffin, Alkylcyclopentane, Alkylcyclohexane, and Alkylbenzene Hydrocarbons,
J. Res. Natl. Bur. Stand. (U.S.), 1945, 35, 3, 219-244, https://doi.org/10.6028/jres.035.009
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Bondi, 1963
Bondi, A.,
Heat of Siblimation of Molecular Crystals: A Catalog of Molecular Structure Increments.,
J. Chem. Eng. Data, 1963, 8, 3, 371-381, https://doi.org/10.1021/je60018a027
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Jones, 1960
Jones, A.H.,
Sublimation Pressure Data for Organic Compounds.,
J. Chem. Eng. Data, 1960, 5, 2, 196-200, https://doi.org/10.1021/je60006a019
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Stull, 1947
Stull, Daniel R.,
Vapor Pressure of Pure Substances. Organic and Inorganic Compounds,
Ind. Eng. Chem., 1947, 39, 4, 517-540, https://doi.org/10.1021/ie50448a022
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Rotinjanz and Nagornow, 1934
Rotinjanz, L.; Nagornow, N.,
Z. Phys. Chem. Abt. A, 1934, 169, 20. [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
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Ruehrwein and Huffman, 1943
Ruehrwein, R.A.; Huffman, H.M.,
Thermal data. XVII. The heat capacity, entropy and free energy of formation of cyclohexane. A new method of heat transfer in low temperature calorimetry,
J. Am. Chem. Soc., 1943, 65, 1620-1625. [all data]
Ziegler and Andrews, 1942
Ziegler, W.T.; Andrews, D.H.,
The heat capacity of benzene-d6,
J. Am. Chem. Soc., 1942, 64, 2482-2485. [all data]
Parks, Huffman, et al., 1930
Parks, G.S.; Huffman, H.M.; Thomas, S.B.,
Thermal data on organic compounds. VI. The heat capacities, entropies and free energies of some saturated, non-benzenoid hydrocarbons,
J. Am. Chem. Soc., 1930, 52, 1032-1041. [all data]
Notes
Go To: Top, Phase change data, References
- Symbols used in this document:
Pc Critical pressure Tboil Boiling point Tc Critical temperature Tfus Fusion (melting) point Ttriple Triple point temperature Vc Critical volume ΔHtrs Enthalpy of phase transition ΔStrs Entropy of phase transition ΔfusH Enthalpy of fusion ΔfusS Entropy of fusion ΔsubH Enthalpy of sublimation ΔvapH Enthalpy of vaporization ΔvapH° Enthalpy of vaporization at standard conditions ΔvapS Entropy of vaporization ρc Critical density - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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