Cyclobutane, octafluoro-
- Formula: C4F8
- Molecular weight: 200.0300
- IUPAC Standard InChIKey: BCCOBQSFUDVTJQ-UHFFFAOYSA-N
- CAS Registry Number: 115-25-3
- 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: Cyclooctafluorobutane; Freon C 318; Freon 318; FC-C 318; Octafluorocyclobutane; Perfluorocyclobutane; Propellant C 318; R C318; Halocarbon C-138; UN 1976; Cyclobutane, 1,1,2,2,3,3,4,4-octafluoro-
- Permanent link for this species. Use this link for bookmarking this species for future reference.
- Information on this page:
- Other data available:
- Data at other public NIST sites:
- Options:
Data at NIST subscription sites:
NIST subscription sites provide data under the NIST Standard Reference Data Program, but require an annual fee to access. The purpose of the fee is to recover costs associated with the development of data collections included in such sites. Your institution may already be a subscriber. Follow the links above to find out more about the data in these sites and their terms of usage.
Gas phase thermochemistry data
Go To: Top, 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 compiled by: Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°gas | Cm | Andreevskii and Antonova, 1982 | uncertain value: -1510. kJ/mol | ||
ΔfH°gas | -1488. | kJ/mol | Ccb | Kolesov, Talakin, et al., 1968 | Correction of Kolesov, Talakin, et al., 1964 |
Condensed phase thermochemistry data
Go To: Top, Gas 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 compiled by: Eugene S. Domalski and Elizabeth D. Hearing
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
S°liquid | 291.1 | J/mol*K | N/A | Furukawa, McCoskey, et al., 1954 |
Constant pressure heat capacity of liquid
Cp,liquid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
222.4 | 296.41 | Ponomareva, 1982 | T = 240 to 340 K. Value is unsmoothed experimental datum: Cp given as 1.112 J/g*K. |
209.77 | 268.52 | Furukawa, McCoskey, et al., 1954 | T = 17 to 270 K. Value is unsmoothed experimental datum. |
Phase change data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry 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 compiled as indicated in comments:
BS - Robert L. Brown and Stephen E. Stein
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, Chris Muzny director
DH - Eugene S. Domalski and Elizabeth D. Hearing
AC - William E. Acree, Jr., James S. Chickos
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 267.3 | K | N/A | PCR Inc., 1990 | BS |
Tboil | 266.88 | K | N/A | Krauss and Stephan, 1989 | Uncertainty assigned by TRC = 0.2 K; TRC |
Tboil | 223. | K | N/A | Park, Benning, et al., 1947 | Uncertainty assigned by TRC = 10. K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 233. | K | N/A | Park, Benning, et al., 1947 | Uncertainty assigned by TRC = 5. K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 232.96 | K | N/A | Krauss and Stephan, 1989 | Uncertainty assigned by TRC = 0.2 K; TRC |
Ttriple | 232.96 | K | N/A | Furukawa, McCoskey, et al., 1954, 2 | Crystal phase 1 phase; Uncertainty assigned by TRC = 0.02 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 388.46 | K | N/A | Krauss and Stephan, 1989 | Uncertainty assigned by TRC = 0.3 K; TRC |
Tc | 388.44 | K | N/A | Mousa, Kay, et al., 1972 | Uncertainty assigned by TRC = 0.2 K; TRC |
Tc | 388.37 | K | N/A | Douslin, Moore, et al., 1959 | Uncertainty assigned by TRC = 0.1 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 27.84 | bar | N/A | Krauss and Stephan, 1989 | Uncertainty assigned by TRC = 0.05 bar; TRC |
Pc | 27.85 | bar | N/A | Mousa, Kay, et al., 1972 | Uncertainty assigned by TRC = 0.0344 bar; TRC |
Pc | 27.775 | bar | N/A | Douslin, Moore, et al., 1959 | Uncertainty assigned by TRC = 0.081 bar; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Vc | 0.325 | l/mol | N/A | Douslin, Moore, et al., 1959 | Uncertainty assigned by TRC = 0.02 l/mol; TRC |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
23.721 | 261.25 | N/A | Furukawa, McCoskey, et al., 1954 | P = 78.78; DH |
23.5 | 304. | A | Stephenson and Malanowski, 1987 | Based on data from 289. to 348. K.; AC |
23.2 | 358. | A | Stephenson and Malanowski, 1987 | Based on data from 343. to 388. K.; AC |
24.9 | 259. | A | Stephenson and Malanowski, 1987 | Based on data from 233. to 274. K. See also Furukawa, McCoskey, et al., 1954, 2.; AC |
25. | 248. | N/A | Kletskii and Petrik, 1967 | Based on data from 233. to 388. K.; AC |
25. | 254. | N/A | Martin, 1962 | Based on data from 234. to 269. K. See also Boublik, Fried, et al., 1984.; AC |
Entropy of vaporization
ΔvapS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
90.80 | 261.25 | Furukawa, McCoskey, et al., 1954 | 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 |
---|---|---|---|---|---|
233. to 388.37 | 4.254 | 1007.399 | -30.205 | Kletskii and Petric, 1967 | Coefficents calculated by NIST from author's data. |
Enthalpy of phase transition
ΔHtrs (kJ/mol) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
2.7682 | 232.96 | crystaline, I | liquid | Furukawa, McCoskey, et al., 1954 | DH |
Entropy of phase transition
ΔStrs (J/mol*K) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
11.89 | 232.96 | crystaline, I | liquid | Furukawa, McCoskey, et al., 1954 | DH |
Henry's Law 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: 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 |
---|---|---|---|---|
0.00025 | Q | N/A | missing citation give several references for the Henry's law constants but don't assign them to specific species. |
References
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Henry's Law data, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Andreevskii and Antonova, 1982
Andreevskii, D.N.; Antonova, Z.A.,
Development of an increment scheme for calculating the thermodynamic properties of organic polyfluoro compounds,
J. Appl. Chem. USSR, 1982, 55, 582-587. [all data]
Kolesov, Talakin, et al., 1968
Kolesov, V.P.; Talakin, O.G.; Skuratov, S.M.,
Enthalpy of formation of some specimens of amorphous carbon,
Russ. J. Phys. Chem. (Engl. Transl.), 1968, 42, 1218-1220. [all data]
Kolesov, Talakin, et al., 1964
Kolesov, V.P.; Talakin, O.G.; Skuratov, S.M.,
Standard enthalpy of formation of perfluorocyclobutane,
Russ. J. Phys. Chem. (Engl. Transl.), 1964, 38, 930-931. [all data]
Furukawa, McCoskey, et al., 1954
Furukawa, G.T.; McCoskey, R.E.; Reilly, M.L.,
Heat capacity, heats of transitions, fusion and vaporization, and vapor pressure of octafluorocyclobutane,
J. Res., 1954, NBS 52, 11-16. [all data]
Ponomareva, 1982
Ponomareva, O.P.,
Study of the isobaric heat capacity of Freon-113 and Freon-C318 in a broad range of parametric conditions, Teplofiz. Svoistva Veshchestv i Materialov,
Moskva, 1982, 16, 64-70. [all data]
PCR Inc., 1990
PCR Inc.,
Research Chemicals Catalog 1990-1991, PCR Inc., Gainesville, FL, 1990, 1. [all data]
Krauss and Stephan, 1989
Krauss, R.; Stephan, K.,
Thermal Conductivity of Refrigerants in a Wide Range of Temperature and Pressure,
J. Phys. Chem. Ref. Data, 1989, 18, 43. [all data]
Park, Benning, et al., 1947
Park, J.D.; Benning, A.F.; Downing, F.B.; Laucius, J.F.; McHarness, R.C.,
Synthesis of Tetrafluoroethylene. Pyrolysis of Monochlorodifluoromethane,
Ind. Eng. Chem., 1947, 39, 343-8. [all data]
Furukawa, McCoskey, et al., 1954, 2
Furukawa, G.T.; McCoskey, R.E.; Reilly, M.L.,
Heat capacity, heats of transitions, fusion, and vaporization, and vapor pressure of octafluorocyclobutane,
J. RES. NATL. BUR. STAN., 1954, 52, 1, 11, https://doi.org/10.6028/jres.052.003
. [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]
Douslin, Moore, et al., 1959
Douslin, D.R.; Moore, R.T.; Waddington, G.,
The pressure-volume-temperature properties of perfluorocyclobutane: equations of state, viral coefficients and intermolecular potential energy functions,
J. Phys. Chem., 1959, 63, 1959. [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]
Kletskii and Petrik, 1967
Kletskii, A.V.; Petrik, L.E.,
Zh. Fiz. Khim., 1967, 41, 5, 1183. [all data]
Martin, 1962
Martin, J.J.,
Thermodynamic Properties of Perfluorocyclobutane.,
J. Chem. Eng. Data, 1962, 7, 1, 68-72, https://doi.org/10.1021/je60012a020
. [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]
Kletskii and Petric, 1967
Kletskii, A.B.; Petric, L.E.,
Dependence of Vapor Pressure of Perfluorocyclobutane,
Zh. Fiz. Khim., 1967, 41, 1183-1184. [all data]
Notes
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Henry's Law data, References
- Symbols used in this document:
Cp,liquid Constant pressure heat capacity of liquid 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 Vc Critical volume d(ln(kH))/d(1/T) Temperature dependence parameter for Henry's Law constant k°H Henry's Law constant at 298.15K ΔHtrs Enthalpy of phase transition ΔStrs Entropy of phase transition ΔfH°gas Enthalpy of formation of gas at standard conditions ΔvapH Enthalpy of vaporization ΔvapS Entropy of vaporization - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
- The National Institute of Standards and Technology (NIST) uses its best efforts to deliver a high quality copy of the Database and to verify that the data contained therein have been selected on the basis of sound scientific judgment. However, NIST makes no warranties to that effect, and NIST shall not be liable for any damage that may result from errors or omissions in the Database.
- Customer support for NIST Standard Reference Data products.