Benzene, hexafluoro-
- Formula: C6F6
- Molecular weight: 186.0546
- IUPAC Standard InChIKey: ZQBFAOFFOQMSGJ-UHFFFAOYSA-N
- CAS Registry Number: 392-56-3
- 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: CP 28; Hexafluorobenzene; Perfluorobenzene; 1,2,3,4,5,6-Hexafluorobenzene
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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
DH - Eugene S. Domalski and Elizabeth D. Hearing
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 353.4 ± 0.3 | K | AVG | N/A | Average of 10 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 278.2 ± 0.2 | K | AVG | N/A | Average of 7 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 278.30 | K | N/A | Messerly and Finke, 1970 | Uncertainty assigned by TRC = 0.02 K; TRC |
Ttriple | 278.14 | K | N/A | Paukov and Glukhikh, 1967 | Crystal phase 1 phase; Uncertainty assigned by TRC = 0.15 K; TRC |
Ttriple | 278.25 | K | N/A | Counsell, Green, et al., 1965 | Uncertainty assigned by TRC = 0.02 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 517. ± 1. | K | AVG | N/A | Average of 9 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 33. ± 3. | bar | AVG | N/A | Average of 6 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Vc | 0.3351 | l/mol | N/A | Douslin, Harrison, et al., 1969 | Uncertainty assigned by TRC = 0.0017 l/mol; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 2.958 | mol/l | N/A | Hales and Townsend, 1974 | Uncertainty assigned by TRC = 0.0029 mol/l; Liquid density determined by magnetically balanced float up to 490 K, see J.L.Hales, 1970-128. Critical D by equation due to Riedel.; TRC |
ρc | 2.65 | mol/l | N/A | Mousa, Kay, et al., 1972 | Uncertainty assigned by TRC = 0.0264 mol/l; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 35.9 ± 0.6 | kJ/mol | AVG | N/A | Average of 9 values; Individual data points |
Reduced pressure boiling point
Tboil (K) | Pressure (bar) | Reference | Comment |
---|---|---|---|
354.7 | 0.991 | Aldrich Chemical Company Inc., 1990 | BS |
354. to 355. | 0.991 | PCR Inc., 1990 | BS |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
31.66 | 353.3 | N/A | Majer and Svoboda, 1985 | |
36.5 | 293. | N/A | Douslin and Osborn, 2002 | Based on data from 275. to 387. K.; AC |
34.4 | 333. | EB | Ambrose, Ewing, et al., 1990 | Based on data from 318. to 376. K.; AC |
31.8 | 425. | N/A | Davies, Ewing, et al., 1988 | Based on data from 403. to 516. K.; AC |
36.5 | 293. | A | Stephenson and Malanowski, 1987 | Based on data from 278. to 354. K.; AC |
33.2 | 363. | A | Stephenson and Malanowski, 1987 | Based on data from 348. to 389. K.; AC |
32.2 | 399. | A | Stephenson and Malanowski, 1987 | Based on data from 384. to 462. K.; AC |
31.8 | 473. | A | Stephenson and Malanowski, 1987 | Based on data from 458. to 517. K.; AC |
35.7 | 308. | N/A | Patrick and Tomes, 1980 | Based on data from 293. to 323. K.; AC |
36.2 | 292. | MM | Findlay, 1969 | Based on data from 278. to 321. K.; AC |
32.2 | 378. | EB | Evans and Tiley, 1966 | Based on data from 363. to 516. K.; AC |
35.1 | 308. | N/A | Patrick and Prosser, 1964 | Based on data from 293. to 356. K.; AC |
35.5 | 308. | N/A | Patrick and Prosser, 1964 | Based on data from 293. to 358. K. See also Boublik, Fried, et al., 1984.; 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)
View plot Requires a JavaScript / HTML 5 canvas capable browser.
Temperature (K) | A (kJ/mol) | β | Tc (K) | Reference | Comment |
---|---|---|---|---|---|
301. to 377. | 55.09 | 0.3016 | 516.7 | Majer and Svoboda, 1985 |
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 |
---|---|---|---|---|---|
353.40 to 516.67 | 4.63127 | 1563.21 | -15.19 | Douslin, Harrison, et al., 1969, 2 | Coefficents calculated by NIST from author's data. |
277.89 to 321.00 | 3.98751 | 1153.509 | -64.352 | Findlay, 1969 | Coefficents calculated by NIST from author's data. |
310.4 to 361.94 | 4.14356 | 1220.117 | -58.543 | Counsell, Green, et al., 1965, 2 | Coefficents calculated by NIST from author's data. |
278.4 to 387.19 | 4.16054 | 1229.449 | -57.503 | Douslin and Osborn, 1965 | Coefficents calculated by NIST from author's data. |
Enthalpy of sublimation
ΔsubH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
49.2 | 263. | A | Stephenson and Malanowski, 1987 | Based on data from 215. to 278. K. See also Douslin and Osborn, 2002.; AC |
49.8 | 253. | IP,A | Scott and Osborn, 1979 | Based on data from 238. to 268. K.; AC |
46.0 | 316. | B | Counsell, Green, et al., 1965 | AC |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
11.585 | 278.30 | Messerly and Finke, 1970, 2 | DH |
11.590 | 278.25 | Counsell, Green, et al., 1965, 2 | DH |
11.59 | 278.3 | Domalski and Hearing, 1996 | AC |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
41.63 | 278.30 | Messerly and Finke, 1970, 2 | DH |
41.65 | 278.25 | Counsell, Green, et al., 1965, 2 | 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.
Messerly and Finke, 1970
Messerly, J.F.; Finke, H.L.,
hexafluorobenzene and 1,3-difluorobenzene low temperature calorimetric studies and chemical thermodynamic properties,
J. Chem. Thermodyn., 1970, 2, 867-80. [all data]
Paukov and Glukhikh, 1967
Paukov, I.E.; Glukhikh, L.K.,
Low temperature specific heats and absolute entropies of hexafluorobenzene and pentafluorochlorobenzene,
Zh. Vses. Khim. O-va. im. D. I. Mendeleeva, 1967, 12, 236-7. [all data]
Counsell, Green, et al., 1965
Counsell, J.F.; Green, J.H.S.; Hales, J.L.; Martin, J.F.,
Thermodynamic properties of fluorine compounds Part 2.-Physical and thermodynamic properties of hexafluorobenzene,
Trans. Faraday Soc., 1965, 61, 212. [all data]
Douslin, Harrison, et al., 1969
Douslin, D.R.; Harrison, R.H.; Moore, R.T.,
Pressure-Volume-Temperature Relations of Hexafluorobenzene,
J. Chem. Thermodyn., 1969, 1, 305-19. [all data]
Hales and Townsend, 1974
Hales, J.L.; Townsend, R.,
Liquid Densities from 293 to 490 K of Eight Fluorinated Aromatic Comp.,
J. Chem. Thermodyn., 1974, 6, 111-6. [all data]
Mousa, Kay, et al., 1972
Mousa, A.H.N.; Kay, W.B.; Kreglewski, A.,
The critical constants of binary mixtures of certain perfluoro-compounds with alkanes,
J. Chem. Thermodyn., 1972, 4, 301-11. [all data]
Aldrich Chemical Company Inc., 1990
Aldrich Chemical Company Inc.,
Catalog Handbook of Fine Chemicals, Aldrich Chemical Company, Inc., Milwaukee WI, 1990, 1. [all data]
PCR Inc., 1990
PCR Inc.,
Research Chemicals Catalog 1990-1991, PCR Inc., Gainesville, FL, 1990, 1. [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]
Douslin and Osborn, 2002
Douslin, D.R.; Osborn, A.,
Pressure measurements in the 0.01-30 torr range with an inclined-piston gauge,
J. Sci. Instrum., 2002, 42, 6, 369-373, https://doi.org/10.1088/0950-7671/42/6/301
. [all data]
Ambrose, Ewing, et al., 1990
Ambrose, D.; Ewing, M.B.; Ghiassee, N.B.; Sanchez Ochoa, J.C.,
The ebulliometric method of vapour-pressure measurement: vapour pressures of benzene, hexafluorobenzene, and naphthalene,
The Journal of Chemical Thermodynamics, 1990, 22, 6, 589-605, https://doi.org/10.1016/0021-9614(90)90151-F
. [all data]
Davies, Ewing, et al., 1988
Davies, D.R.; Ewing, M.B.; Hugill, J.A.; McGlashan, M.L.,
The critical temperature, the critical pressure, and the dependence of vapour pressure on temperature for dodecafluorocyclohexane and hexafluorobenzene,
Can. J. Chem., 1988, 66, 4, 760-762, https://doi.org/10.1139/v88-131
. [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]
Patrick and Tomes, 1980
Patrick, C.R.; Tomes, F.,
The vapour pressures and excess free energies of mixing of the systems hexafluorobenzene-carbon tetrachloride and hexafluorobenzene-perfluoromethylcyclohexane,
Journal of Fluorine Chemistry, 1980, 15, 4, 267-278, https://doi.org/10.1016/S0022-1139(00)81462-1
. [all data]
Findlay, 1969
Findlay, T.J.V.,
Vapor pressures of fluorobenzenes from 5 to 50.deg.C,
J. Chem. Eng. Data, 1969, 14, 2, 229-231, https://doi.org/10.1021/je60041a012
. [all data]
Evans and Tiley, 1966
Evans, F.D.; Tiley, P.F.,
Vapour pressures and critical constants of hexafluoro-, pentafluoro-, chloropentafluoro-, and bromopentafluoro-benzene,
J. Chem. Soc., B:, 1966, 134, https://doi.org/10.1039/j29660000134
. [all data]
Patrick and Prosser, 1964
Patrick, C.R.; Prosser, G.S.,
Vapour pressures and related properties of hexafluorobenzene and of pentafluorobenzene,
Trans. Faraday Soc., 1964, 60, 700, https://doi.org/10.1039/tf9646000700
. [all data]
Boublik, Fried, et al., 1984
Boublik, T.; Fried, V.; Hala, E.,
The Vapour Pressures of Pure Substances: Selected Values of the Temperature Dependence of the Vapour Pressures of Some Pure Substances in the Normal and Low Pressure Region, 2nd ed., Elsevier, New York, 1984, 972. [all data]
Douslin, Harrison, et al., 1969, 2
Douslin, D.R.; Harrison, R.H.; Moore, R.T.,
Pressure-Volume-Temperature Relations of Hexafluorobenzene,
J. Chem. Thermodyn., 1969, 1, 3, 305-319, https://doi.org/10.1016/0021-9614(69)90050-0
. [all data]
Counsell, Green, et al., 1965, 2
Counsell, J.F.; Green, J.H.S.; Hales, J.L.; Martin, J.F.,
Thermodynamic properties of fluorine compounds. Part 2. Physical and thermodynamic properties of hexafluorobenzene,
Trans. Faraday Soc., 1965, 61, 212-218. [all data]
Douslin and Osborn, 1965
Douslin, D.R.; Osborn, A.,
Pressure Measurements in the 0·01-30 Torr with an Inclined-Piston Gauge,
J. Sci. Instrum., 1965, 42, 6, 369-373, https://doi.org/10.1088/0950-7671/42/6/301
. [all data]
Scott and Osborn, 1979
Scott, D.W.; Osborn, A.G.,
Representation of vapor-pressure data,
J. Phys. Chem., 1979, 83, 21, 2714-2723, https://doi.org/10.1021/j100484a007
. [all data]
Messerly and Finke, 1970, 2
Messerly, J.F.; Finke, H.L.,
Hexafluorobenzene and 1,3-difluorobenzene. Low-temperature calorimetric studies and chemical thermodynamic properties,
J. Chem. Thermodynam., 1970, 2, 867-880. [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]
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 ΔfusH Enthalpy of fusion ΔfusS Entropy of fusion 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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