Anisole
- Formula: C7H8O
- Molecular weight: 108.1378
- IUPAC Standard InChIKey: RDOXTESZEPMUJZ-UHFFFAOYSA-N
- CAS Registry Number: 100-66-3
- 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: Benzene, methoxy-; Anizol; Methoxybenzene; Methyl phenyl ether; Phenyl methyl ether; Ether, methyl phenyl-; UN 2222; Phenoxymethane; Anisol; NSC 7920
- Permanent link for this species. Use this link for bookmarking this species for future reference.
- Information on this page:
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Condensed phase thermochemistry data
Go To: Top, Phase change data, Henry's Law data, Gas phase ion energetics 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 | -114.8 ± 1.2 | kJ/mol | Ccb | Fenwick, Harrop, et al., 1975 | Author was aware that data differs from previously reported values; ALS |
ΔfH°liquid | -120. ± 0.8 | kJ/mol | Ccb | Lebedeva and Katin, 1972 | ALS |
ΔfH°liquid | -118.4 | kJ/mol | Ccb | Badoche, 1941 | Author's hf298_condensed=-31.02 kcal/mol; ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -3783.12 | kJ/mol | Ccb | Fenwick, Harrop, et al., 1975 | Author was aware that data differs from previously reported values; Corresponding ΔfHºliquid = -114.77 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -3778. ± 0.8 | kJ/mol | Ccb | Lebedeva and Katin, 1972 | Corresponding ΔfHºliquid = -120. kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -3779.5 | kJ/mol | Ccb | Badoche, 1941 | Author's hf298_condensed=-31.02 kcal/mol; Corresponding ΔfHºliquid = -118.4 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
Constant pressure heat capacity of liquid
Cp,liquid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
199.0 | 298.15 | Fenwick, Harrop, et al., 1975, 2 | DH |
208.8 | 304.8 | Phillip, 1939 | DH |
191.2 | 297.2 | de Kolossowsky and Udowenko, 1933 | DH |
Phase change data
Go To: Top, Condensed phase thermochemistry data, Henry's Law data, Gas phase ion energetics 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
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
DRB - Donald R. Burgess, Jr.
DH - Eugene S. Domalski and Elizabeth D. Hearing
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 427.0 ± 0.9 | K | AVG | N/A | Average of 19 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 250. ± 40. | K | AVG | N/A | Average of 9 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 643. ± 4. | K | AVG | N/A | Average of 6 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 42.0 ± 0.5 | bar | AVG | N/A | Average of 6 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 2.93 | mol/l | N/A | Wilson, Wilson, et al., 1996 | Uncertainty assigned by TRC = 0.092 mol/l; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 44. ± 7. | kJ/mol | AVG | N/A | Average of 13 values; Individual data points |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
38.97 | 426.8 | N/A | Majer and Svoboda, 1985 | |
41.8 | 397. | N/A | Reich and Sanhueza, 1993 | Based on data from 382. to 429. K.; AC |
41.9 | 397. | A | Stephenson and Malanowski, 1987 | Based on data from 382. to 437. K. See also Ambrose, Ellender, et al., 1976.; AC |
39.0 | 426. | N/A | Ambrose, Ellender, et al., 1976 | Based on data from 282. to 437. K.; AC |
42.9 ± 0.1 | 367. | C | Hales, Lees, et al., 1967 | AC |
42.0 ± 0.1 | 382. | C | Hales, Lees, et al., 1967 | AC |
40.5 ± 0.1 | 402. | C | Hales, Lees, et al., 1967 | AC |
38.9 ± 0.1 | 427. | C | Hales, Lees, et al., 1967 | AC |
41.9 | 397. | N/A | von Terres, Gebert, et al., 1955 | Based on data from 382. to 437. K. See also Collerson, Counsell, et al., 1965.; 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 |
---|---|---|---|---|---|
298. to 427. | 63.45 | 0.2787 | 644.1 | 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 |
---|---|---|---|---|
383.03 to 437.26 | 4.17726 | 1489.756 | -69.607 | Collerson, Counsell, et al., 1965, 2 |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
11.66 | 237. | Domalski and Hearing, 1996 | See also Lee, Lien, et al., 1994.; AC |
12.89 | 236. | Domalski and Hearing, 1996 | AC |
17.029 | 293.2 | Eykman, 1889 | DH |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
58.1 | 293.2 | Eykman, 1889 | DH |
Enthalpy of phase transition
ΔHtrs (kJ/mol) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
12.890 | 268.73 | crystaline, I | liquid | Goates, Boerio-Goates, et al., 1987 | DH |
Entropy of phase transition
ΔStrs (J/mol*K) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
48.0 | 268.73 | crystaline, I | liquid | Goates, Boerio-Goates, et al., 1987 | DH |
Henry's Law 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 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 |
---|---|---|---|
0.24 | V | N/A | |
0.24 | R | N/A |
Gas phase ion energetics 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 evaluated as indicated in comments:
HL - Edward P. Hunter and Sharon G. Lias
L - Sharon G. Lias
Data compiled as indicated in comments:
B - John E. Bartmess
LBLHLM - Sharon G. Lias, John E. Bartmess, Joel F. Liebman, John L. Holmes, Rhoda D. Levin, and W. Gary Mallard
LLK - Sharon G. Lias, Rhoda D. Levin, and Sherif A. Kafafi
RDSH - Henry M. Rosenstock, Keith Draxl, Bruce W. Steiner, and John T. Herron
View reactions leading to C7H8O+ (ion structure unspecified)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
IE (evaluated) | 8.20 ± 0.05 | eV | N/A | N/A | L |
Quantity | Value | Units | Method | Reference | Comment |
Proton affinity (review) | 839.6 | kJ/mol | N/A | Hunter and Lias, 1998 | HL |
Quantity | Value | Units | Method | Reference | Comment |
Gas basicity | 807.2 | kJ/mol | N/A | Hunter and Lias, 1998 | HL |
Ionization energy determinations
IE (eV) | Method | Reference | Comment |
---|---|---|---|
8.25 ± 0.03 | PI | Ponomarev, Arapov, et al., 1986 | LBLHLM |
~8.10 | PE | Klasinc, Kovac, et al., 1983 | LBLHLM |
8.24 | PE | Behan, Johnstone, et al., 1976 | LLK |
8.6 | EI | McLafferty, Bente, et al., 1973 | LLK |
8.20 ± 0.02 | PE | Maier and Turner, 1973 | LLK |
8.37 | CTS | Kobayashi, Kobayashi, et al., 1973 | LLK |
8.3 ± 0.1 | EI | Gilbert, Leach, et al., 1973 | LLK |
8.20 | EI | Cooks, Bertrand, et al., 1973 | LLK |
8.18 | CTS | Pitt, Carey, et al., 1972 | LLK |
8.8 ± 0.1 | EI | Gross, 1972 | LLK |
8.4 ± 0.1 | EI | Brown, 1970 | RDSH |
8.21 | PE | Dewar and Worley, 1969 | RDSH |
8.6 | EI | Williams, Cooks, et al., 1968 | RDSH |
8.22 ± 0.02 | PI | Watanabe, Nakayama, et al., 1962 | RDSH |
8.20 ± 0.02 | PI | Watanabe, 1957 | RDSH |
8.39 | PE | Klasinc, Kovac, et al., 1983 | Vertical value; LBLHLM |
8.45 | PE | Friege and Klessinger, 1979 | Vertical value; LLK |
8.42 | PE | Kobayashi, 1978 | Vertical value; LLK |
8.25 | PE | Benoit and Harrison, 1977 | Vertical value; LLK |
8.39 | PE | Kobayashi and Nagakura, 1974 | Vertical value; LLK |
8.46 | PE | Dewar, Ernstbrunner, et al., 1974 | Vertical value; LLK |
8.42 | PE | Bock and Wagner, 1972 | Vertical value; LLK |
Appearance energy determinations
Ion | AE (eV) | Other Products | Method | Reference | Comment |
---|---|---|---|---|---|
C5H5+ | 13.1 ± 0.1 | CH3+CO | PIPECO | Das, Gilman, et al., 1986 | LBLHLM |
C5H5+ | 13.5 | ? | EI | Harrison, Haynes, et al., 1965 | RDSH |
C6H5O+ | 11.70 ± 0.05 | CH3 | PI | Ponomarev, Arapov, et al., 1986 | LBLHLM |
C6H5O+ | 11.9 ± 0.1 | CH3 | PIPECO | Das, Gilman, et al., 1986 | LBLHLM |
C6H5O+ | 11.3 | CH3 | EI | McLafferty, Bente, et al., 1973 | LLK |
C6H5O+ | 11.8 ± 0.1 | CH3 | EI | Brown, 1970 | RDSH |
C6H5O+ | 11.9 ± 0.1 | CH3 | EI | Fisher, Palmer, et al., 1964 | RDSH |
C6H5O+ | 11.9 ± 0.1 | CH3 | EI | Tait, Shannon, et al., 1962 | RDSH |
C6H6+ | 10.85 ± 0.05 | CH2O | PI | Ziesel and Lifshitz, 1987 | LBLHLM |
C6H6+ | 11.4 ± 0.1 | CH2O | PIPECO | Das, Gilman, et al., 1986 | LBLHLM |
C6H6+ | 11.50 | HCHO | EI | Cooks, Bertrand, et al., 1973 | LLK |
C6H6+ | 11.6 ± 0.1 | HCHO | EI | Gross, 1972 | LLK |
C6H6+ | 11.3 ± 0.1 | CH2O | EI | Brown, 1970 | RDSH |
C6H6+ | 11.30 | ? | EI | Howe and Williams, 1969 | RDSH |
C6H7+ | 12.1 ± 0.1 | CHO | PIPECO | Das, Gilman, et al., 1986 | LBLHLM |
C6H7+ | 12.1 | CO+H? | EI | Harrison, Haynes, et al., 1965 | RDSH |
De-protonation reactions
C7H7O- + =
By formula: C7H7O- + H+ = C7H8O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1679. ± 13. | kJ/mol | G+TS | Dahlke and Kass, 1992 | gas phase; Acid: anisole. Between o-methoxyphenide and Me2NH.; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1648. ± 13. | kJ/mol | IMRB | Dahlke and Kass, 1992 | gas phase; Acid: anisole. Between o-methoxyphenide and Me2NH.; B |
C7H7O- + =
By formula: C7H7O- + H+ = C7H8O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1666. ± 13. | kJ/mol | G+TS | Dahlke and Kass, 1992 | gas phase; Acid: anisole. Between HO- and m,p-methoxyphenide; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1636. ± 13. | kJ/mol | IMRB | Dahlke and Kass, 1992 | gas phase; Acid: anisole. Between HO- and m,p-methoxyphenide; B |
C7H7O- + =
By formula: C7H7O- + H+ = C7H8O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1681. ± 13. | kJ/mol | G+TS | Dahlke and Kass, 1992 | gas phase; Acid: anisole. Between o-OMe-phenide and Me2NH.; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1648. ± 13. | kJ/mol | IMRB | Dahlke and Kass, 1992 | gas phase; Acid: anisole. Between o-OMe-phenide and Me2NH.; B |
References
Go To: Top, Condensed phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics data, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Fenwick, Harrop, et al., 1975
Fenwick, J.O.; Harrop, D.; Head, A.J.,
Thermodynamic properties of organic oxygen compounds. 41. Enthalpies of formation of eight ethers,
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Heats of combustion of certain monosubstituted benzenes,
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No 19. - Chaleurs de combustion du phenol, du-m-cresol et del leurs ethers; par M. Marius BADOCHE.,
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Mesure des chaleurs specifique moleculaires de quelques liquides,
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Critical Point Measurements for Fourteen Compounds by a Static Method and a Flow Method,
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Vapor-liquid equilibria for .alpha.-pinene or .beta.-pinene with anisole,
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Photoelectron spectra of substituted benzenes,
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Howe and Williams, 1969
Howe, I.; Williams, D.H.,
Calculation and qualitative predictions of mass spectra. Mono- and paradisubstituted benzenes,
J. Am. Chem. Soc., 1969, 91, 7137. [all data]
Dahlke and Kass, 1992
Dahlke, G.D.; Kass, S.R.,
The Ortho-dehydrophenoxy Anion,
Int. J. Mass Spectrom. Ion Proc., 1992, 117, 633, https://doi.org/10.1016/0168-1176(92)80117-J
. [all data]
Notes
Go To: Top, Condensed phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics data, References
- Symbols used in this document:
AE Appearance energy Cp,liquid Constant pressure heat capacity of liquid IE (evaluated) Recommended ionization energy Pc Critical pressure Tboil Boiling point Tc Critical temperature Tfus Fusion (melting) point 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 ΔcH°liquid Enthalpy of combustion of liquid at standard conditions ΔfH°liquid Enthalpy of formation of liquid at standard conditions ΔfusH Enthalpy of fusion ΔfusS Entropy of fusion ΔrG° Free energy of reaction at standard conditions ΔrH° Enthalpy of reaction at standard conditions 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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