Methyl fluoride
- Formula: CH3F
- Molecular weight: 34.0329
- IUPAC Standard InChIKey: NBVXSUQYWXRMNV-UHFFFAOYSA-N
- CAS Registry Number: 593-53-3
- 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: Fluoromethane; Methane, fluoro-; Freon 41; CH3F; UN 2454; R 41; HFC-41; Refrigerant gas R 41
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Gas phase thermochemistry data
Go To: Top, Phase change data, Reaction 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:
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°gas | -234.30 | kJ/mol | Review | Chase, 1998 | Data last reviewed in December, 1963 |
ΔfH°gas | -247. | kJ/mol | Ion | Lias, Karpas, et al., 1985 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
S°gas,1 bar | 222.84 | J/mol*K | Review | Chase, 1998 | Data last reviewed in December, 1963 |
Gas Phase Heat Capacity (Shomate Equation)
Cp° = A + B*t + C*t2 + D*t3 +
E/t2
H° − H°298.15= A*t + B*t2/2 +
C*t3/3 + D*t4/4 − E/t + F − H
S° = A*ln(t) + B*t + C*t2/2 + D*t3/3 −
E/(2*t2) + G
Cp = heat capacity (J/mol*K)
H° = standard enthalpy (kJ/mol)
S° = standard entropy (J/mol*K)
t = temperature (K) / 1000.
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Temperature (K) | 298. to 1200. | 1200. to 6000. |
---|---|---|
A | -8.802593 | 88.64892 |
B | 154.8561 | 10.09951 |
C | -91.15011 | -1.937578 |
D | 21.55007 | 0.128915 |
E | 0.680703 | -21.52898 |
F | -235.5169 | -307.0345 |
G | 173.7096 | 270.0345 |
H | -234.3044 | -234.3044 |
Reference | Chase, 1998 | Chase, 1998 |
Comment | Data last reviewed in December, 1963 | Data last reviewed in December, 1963 |
Phase change data
Go To: Top, Gas phase thermochemistry data, Reaction 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:
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
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 195. | K | N/A | Papousek, Tesar, et al., 1991 | Uncertainty assigned by TRC = 2. K; TRC |
Tboil | 194.6 | K | N/A | PCR Inc., 1990 | BS |
Tboil | 195. | K | N/A | Filatov, Makarov, et al., 1968 | Uncertainty assigned by TRC = 2. K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Ptriple | 0.00370 | bar | N/A | Fonseca and Lobo, 1989 | Uncertainty assigned by TRC = 0.00005 bar; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 317.4 | K | N/A | Bominaar, Biswas, et al., 1987 | Uncertainty assigned by TRC = 0.5 K; PVT by Burnett method. R41; TRC |
Tc | 317.7 | K | N/A | Cawood and Patterson, 1932 | Uncertainty assigned by TRC = 0.05 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 58.70 | bar | N/A | Bominaar, Biswas, et al., 1987 | Uncertainty assigned by TRC = 0.5865 bar; PVT by Burnett method. R41; TRC |
Pc | 58.7685 | bar | N/A | Cawood and Patterson, 1932 | Uncertainty assigned by TRC = 0.2026 bar; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 9.20 | mol/l | N/A | Biswas, Ten Seldam, et al., 1989 | Uncertainty assigned by TRC = 0.06 mol/l; from equation of state fit to obs. density; TRC |
ρc | 9.17 | mol/l | N/A | Biswas, Ten Seldam, et al., 1989 | Uncertainty assigned by TRC = 0.06 mol/l; from extraplation of rectilinear diameter; TRC |
ρc | 9.14 | mol/l | N/A | Bominaar, Biswas, et al., 1987 | Uncertainty assigned by TRC = 0.0091 mol/l; PVT by Burnett Method, R41. Original units mol m-3; TRC |
ρc | 8.824 | mol/l | N/A | Cawood and Patterson, 1932 | Uncertainty assigned by TRC = 0.009 mol/l; TRC |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
16.9 | 227. | A | Stephenson and Malanowski, 1987 | Based on data from 205. to 242. K.; AC |
16.9 | 273. | A | Stephenson and Malanowski, 1987 | Based on data from 240. to 288. K.; AC |
17.1 | 193. | A,E | Stephenson and Malanowski, 1987 | Based on data from 141. to 208. K. See also Li and Rossini, 1961 and Dykyj, 1970.; AC |
16.4 | 202. | N/A | Stephenson and Malanowski, 1987 | Based on data from 165. to 217. K. See also Michels and Wassenaar, 1948 and Boublik, Fried, et al., 1984.; AC |
17.7 | 183. | A | Stephenson and Malanowski, 1987 | Based on data from 170. to 197. K. See also Moles and Batuecas, 1919 and Boublik, Fried, et al., 1984.; AC |
17.9 | 172. | N/A | Oi, Shulman, et al., 1983 | Based on data from 133. to 211. 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 | Comment |
---|---|---|---|---|---|
164.26 to 216.77 | 3.0514 | 395.889 | -64.151 | Michels and Wassenaar, 1948 | Coefficents calculated by NIST from author's data. |
Reaction 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 as indicated in comments:
B - John E. Bartmess
M - Michael M. Meot-Ner (Mautner) and Sharon G. Lias
MS - José A. Martinho Simões
RCD - Robert C. Dunbar
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: Cl- + CH3F = (Cl- • CH3F)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 48.1 ± 8.4 | kJ/mol | IMRE | Larson and McMahon, 1984 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 84.9 | J/mol*K | N/A | Larson and McMahon, 1984 | gas phase; switching reaction(Cl-)CH3Cl, Entropy change calculated or estimated; Larson and McMahon, 1984, 2; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 23. | kJ/mol | ICR | Larson and McMahon, 1984 | gas phase; switching reaction(Cl-)CH3Cl, Entropy change calculated or estimated; Larson and McMahon, 1984, 2; M |
CH2F- + =
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1756. ± 19. | kJ/mol | EIAE | Rogers, Simpson, et al., 2010 | gas phase; B |
ΔrH° | 1711. ± 17. | kJ/mol | CIDT | Graul and Squires, 1990 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1676. ± 17. | kJ/mol | H-TS | Graul and Squires, 1990 | gas phase; B |
By formula: HO2S+ + CH3F = (HO2S+ • CH3F)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 106. | kJ/mol | PHPMS | McMahon and Kebarle, 1986 | gas phase; switching reaction(SO2H+)SO2; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 119. | J/mol*K | PHPMS | McMahon and Kebarle, 1986 | gas phase; switching reaction(SO2H+)SO2; M |
By formula: CH3+ + CH3F = (CH3+ • CH3F)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 230. | kJ/mol | PHPMS | McMahon, Heinis, et al., 1988 | gas phase; switching reaction(CH3+)N2, Entropy change calculated or estimated, uses MCA(N2) = 202. kJ/mol; Foster, Williamson, et al., 1974; M |
By formula: Li+ + CH3F = (Li+ • CH3F)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 130. | kJ/mol | ICR | Staley and Beauchamp, 1975 | gas phase; switching reaction(Li+)H2O, from graph; Dzidic and Kebarle, 1970 interpolated; M |
By formula: CH6N+ + CH3F = (CH6N+ • CH3F)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 49.4 | kJ/mol | PHPMS | Meot-Ner, 1984 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 97.5 | J/mol*K | PHPMS | Meot-Ner, 1984 | gas phase; M |
By formula: CH4F+ + CH3F = (CH4F+ • CH3F)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 130. ± 8. | kJ/mol | PHPMS | McMahon and Kebarle, 1986 | gas phase; switching reaction(SO2H+)SO2; Lias, Liebman, et al., 1984; M |
C5O5W (g) + (g) = C6H3FO5W (g)
By formula: C5O5W (g) + CH3F (g) = C6H3FO5W (g)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -47. ± 13. | kJ/mol | EqG | Brown, Ishikawa, et al., 1990 | Temperature range: ca. 300-350 K; MS |
By formula: Al+ + CH3F = (Al+ • CH3F)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 90.0 ± 8.4 | kJ/mol | EqG | Bouchard, Brenner, et al., 1997 | RCD |
Henry's Law 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 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 |
---|---|---|---|---|
0.071 | Q | N/A | missing citation give several references for the Henry's law constants but don't assign them to specific species. Value at T = 288. K. | |
0.052 | L | N/A | ||
0.059 | 2200. | L | N/A | |
0.059 | V | N/A |
References
Go To: Top, Gas phase thermochemistry data, Phase change data, Reaction thermochemistry 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.
Chase, 1998
Chase, M.W., Jr.,
NIST-JANAF Themochemical Tables, Fourth Edition,
J. Phys. Chem. Ref. Data, Monograph 9, 1998, 1-1951. [all data]
Lias, Karpas, et al., 1985
Lias, S.G.; Karpas, Z.; Liebman, J.F.,
Halomethylenes: effects of halogen substitution on absolute heats of formation,
J. Am. Chem. Soc., 1985, 107, 6089-6096. [all data]
Papousek, Tesar, et al., 1991
Papousek, D.; Tesar, R.; Pracna, P.; Civis, S.; Winnewisser, M.; Belov, S.P.; Tret'yakov, M.Y.,
High-resolution Fourier transform and submillimeter-wave study of the ν6 band of methyl-12C fluoride,
J. Mol. Spectrosc., 1991, 147, 279-99. [all data]
PCR Inc., 1990
PCR Inc.,
Research Chemicals Catalog 1990-1991, PCR Inc., Gainesville, FL, 1990, 1. [all data]
Filatov, Makarov, et al., 1968
Filatov, A.S.; Makarov, S.P.; Yakubovich, A.Ya.,
Halogenation of 1,1,1-Trifluoroazomethane,
Zh. Obshch. Khim., 1968, 38, 33. [all data]
Fonseca and Lobo, 1989
Fonseca, I.M.A.; Lobo, L.Q.,
Thermodynamics of liquid mixtures of xenon and methyl fluoride,
Fluid Phase Equilib., 1989, 47, 249. [all data]
Bominaar, Biswas, et al., 1987
Bominaar, S.A.R.C.; Biswas, S.N.; Trappeniers, N.J.; Ten Seldam, C.A.,
(p, Vm, T) properties of methyl fluoride in the (gas + liquid) critical region,
J. Chem. Thermodyn., 1987, 19, 959. [all data]
Cawood and Patterson, 1932
Cawood, W.; Patterson, H.S.,
Some Physical Constants of Methyl Fluoride, and the Atomic Weight of Fluorine,
J. Chem. Soc., 1932, 1932, 2180. [all data]
Biswas, Ten Seldam, et al., 1989
Biswas, S.N.; Ten Seldam, C.A.; Bominaar, S.A.R.C.; Trappeniers, N.J.,
Liquid-vapor coexistence curve of methyl fluoride in the critical region,
Fluid Phase Equilib., 1989, 49, 1-7. [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]
Li and Rossini, 1961
Li, J.C.M.; Rossini, F.D.,
Vapor Pressures and Boiling Points of the l-Fluoroalkanes, l-Chloroalkanes, l-Bromoalkanes, and l-Iodoalkanes, C 1 to C 20 .,
J. Chem. Eng. Data, 1961, 6, 2, 268-270, https://doi.org/10.1021/je60010a025
. [all data]
Dykyj, 1970
Dykyj, J.,
Petrochemica, 1970, 10, 2, 51. [all data]
Michels and Wassenaar, 1948
Michels, A.; Wassenaar, T.,
Vapour pressure of methylfluoride,
Physica, 1948, 14, 2-3, 104-110, https://doi.org/10.1016/0031-8914(48)90030-5
. [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]
Moles and Batuecas, 1919
Moles, E.; Batuecas, T.J.,
J. Chim. Phys. Phys.-Chim. Biol., 1919, 17, 537. [all data]
Oi, Shulman, et al., 1983
Oi, Takao; Shulman, Jan; Popowicz, Anthony; Ishida, Takanobu,
Vapor pressure isotope effects in liquid methyl fluoride,
J. Phys. Chem., 1983, 87, 16, 3153-3160, https://doi.org/10.1021/j100239a038
. [all data]
Larson and McMahon, 1984
Larson, J.W.; McMahon, T.B.,
Hydrogen bonding in gas phase anions. An experimental investigation of the interaction between chloride ion and bronsted acids from ICR chloride exchange equilibria,
J. Am. Chem. Soc., 1984, 106, 517. [all data]
Larson and McMahon, 1984, 2
Larson, J.W.; McMahon, T.B.,
Gas phase negative ion chemistry of alkylchloroformates,
Can. J. Chem., 1984, 62, 675. [all data]
Rogers, Simpson, et al., 2010
Rogers, N.J.; Simpson, M.J.; Tuckett, R.P.; Dunn, K.F.; Latimer, C.J.,
Vacuum-UV negative photoion spectroscopy of CH3F, CH3Cl and CH3Br,
Phys. Chem. Chem. Phys., 2010, 12, 36, 10971-10980, https://doi.org/10.1039/c0cp00234h
. [all data]
Graul and Squires, 1990
Graul, S.T.; Squires, R.R.,
Gas-Phase Acidities Derived from Threshold Energies for Activated Reactions,
J. Am. Chem. Soc., 1990, 112, 7, 2517, https://doi.org/10.1021/ja00163a007
. [all data]
McMahon and Kebarle, 1986
McMahon, T.B.; Kebarle, P.,
Strong hydrogen bonding in gas-phase ions: A high pressure mass spectrometric study of formation and energetics of methyl fluoride proton bound dimer,
J. Am. Chem. Soc., 1986, 108, 6502. [all data]
McMahon, Heinis, et al., 1988
McMahon, T.; Heinis, T.; Nicol, G.; Hovey, J.K.; Kebarle, P.,
Methyl Cation Affinities,
J. Am. Chem. Soc., 1988, 110, 23, 7591, https://doi.org/10.1021/ja00231a002
. [all data]
Foster, Williamson, et al., 1974
Foster, M.S.; Williamson, A.D.; Beauchamp, J.L.,
Photoionization mass spectrometry of trans-azomethane,
Int. J. Mass Spectrom. Ion Phys., 1974, 15, 429. [all data]
Staley and Beauchamp, 1975
Staley, R.H.; Beauchamp, J.L.,
Intrinsic Acid - Base Properties of Molecules. Binding Energies of Li+ to pi - and n - Donor Bases,
J. Am. Chem. Soc., 1975, 97, 20, 5920, https://doi.org/10.1021/ja00853a050
. [all data]
Dzidic and Kebarle, 1970
Dzidic, I.; Kebarle, P.,
Hydration of the Alkali Ions in the Gas Phase. Enthalpies and Entropies of Reactions M+(H2O)n-1 + H2O = M+(H2O)n,
J. Phys. Chem., 1970, 74, 7, 1466, https://doi.org/10.1021/j100702a013
. [all data]
Meot-Ner, 1984
Meot-Ner, (Mautner)M.,
The Ionic Hydrogen Bond and Ion Solvation. 1. -NH+ O-, -NH+ N- and -OH+ O- Bonds. Correlations with Proton Affinity. Deviations Due to Structural Effects,
J. Am. Chem. Soc., 1984, 106, 5, 1257, https://doi.org/10.1021/ja00317a015
. [all data]
Lias, Liebman, et al., 1984
Lias, S.G.; Liebman, J.F.; Levin, R.D.,
Evaluated gas phase basicities and proton affinities of molecules heats of formation of protonated molecules,
J. Phys. Chem. Ref. Data, 1984, 13, 695. [all data]
Brown, Ishikawa, et al., 1990
Brown, C.E.; Ishikawa, Y.; Hackett, P.A.; Rayner, D.M.,
J. Am. Chem. Soc., 1990, 112, 2530. [all data]
Bouchard, Brenner, et al., 1997
Bouchard, F.; Brenner, V.; Carra, C.; Hepburn, J.W.; Koyanagi, G.K.; McMahon, T.B.; Ohanessian, G.; Peschke, M.,
Energetics and Structure of Complexes of Al+ with Small Organic Molecules in the Gas Phase,
J. Phys. Chem. A, 1997, 101, 33, 5885, https://doi.org/10.1021/jp9703465
. [all data]
Notes
Go To: Top, Gas phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, References
- Symbols used in this document:
Pc Critical pressure Ptriple Triple point pressure S°gas,1 bar Entropy of gas at standard conditions (1 bar) Tboil Boiling point Tc Critical temperature d(ln(kH))/d(1/T) Temperature dependence parameter for Henry's Law constant k°H Henry's Law constant at 298.15K ΔfH°gas Enthalpy of formation of gas at standard conditions ΔrG° Free energy of reaction at standard conditions ΔrH° Enthalpy of reaction at standard conditions ΔrS° Entropy of reaction at standard conditions ΔvapH Enthalpy of vaporization ρc Critical density - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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