Formic acid
- Formula: CH2O2
- Molecular weight: 46.0254
- IUPAC Standard InChIKey: BDAGIHXWWSANSR-UHFFFAOYSA-N
- CAS Registry Number: 64-18-6
- 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: Methanoic acid; Aminic acid; Bilorin; Collo-Bueglatt; Collo-Didax; Formisoton; Formylic acid; Hydrogen carboxylic acid; Myrmicyl; HCOOH; Acide formique; Acido formico; Ameisensaeure; Kwas metaniowy; Kyselina mravenci; Mierenzuur; Rcra waste number U123; UN 1779; Formira; Add-F; Amasil
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Gas phase thermochemistry data
Go To: Top, Reaction thermochemistry data, Gas phase ion energetics data, Ion clustering data, Gas Chromatography, 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
DRB - Donald R. Burgess, Jr.
GT - Glushko Thermocenter, Russian Academy of Sciences, Moscow
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°gas | -90.49 | kcal/mol | Cm | Guthrie, 1974 | Heat of hydrolysis; ALS |
ΔfH°gas | -90.58 | kcal/mol | N/A | Lebedeva, 1964 | Value computed using ΔfHliquid° value of -425.5±0.3 kj/mol from Lebedeva, 1964 and ΔvapH° value of 46.5 kj/mol from Guthrie, 1974.; DRB |
ΔfH°gas | -90.6 ± 0.1 | kcal/mol | Ccb | Lebedeva, 1964 | Value computed using ΔfHliquid° from Lebedeva, 1964 and ΔvapH° value of 11.1 kcal/mol from Konicek and Wadso, 1970.; DRB |
ΔfH°gas | -90.42 | kcal/mol | N/A | Sinke, 1959 | Value computed using ΔfHliquid° value of -424.8±0.3 kj/mol from Sinke, 1959 and ΔvapH° value of 46.5 kj/mol from Guthrie, 1974.; DRB |
ΔfH°gas | -90.5 ± 0.1 | kcal/mol | Ccb | Sinke, 1959 | Value computed using ΔfHliquid° from Sinke, 1959 and ΔvapH° value of 11.1 kcal/mol from Konicek and Wadso, 1970.; DRB |
Quantity | Value | Units | Method | Reference | Comment |
S°gas | 59.44 ± 0.10 | cal/mol*K | N/A | Millikan R.C., 1957 | Other third-law S(298.15 K) value is 248.11(1.26) J/mol*K [ Halford J.O., 1942, Millikan R.C., 1957]. Please also see Waring W., 1952.; GT |
Constant pressure heat capacity of gas
Cp,gas (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
7.949 | 50. | Chao J., 1986 | p=1 bar. Selected entropies and heat capacities are in close agreement with statistically calculated values [ Fukushima K., 1971] and value of S(298.15 K) calculated by ab initio method [ East A.L.L., 1997]. Maximum discrepancies with other statistical calculations [ Waring W., 1952, Green J.H.S., 1961, Gurvich, Veyts, et al., 1989] amount to 1.1-3.9 J/mol*K for S(T) and 3.0-5.9 J/mol*K for Cp(T). Please also see Chao J., 1978.; GT |
7.992 | 100. | ||
8.344 | 150. | ||
9.042 | 200. | ||
10.41 | 273.15 | ||
10.92 ± 0.02 | 298.15 | ||
10.96 | 300. | ||
13.03 | 400. | ||
14.97 | 500. | ||
16.68 | 600. | ||
18.17 | 700. | ||
19.44 | 800. | ||
20.50 | 900. | ||
21.37 | 1000. | ||
22.07 | 1100. | ||
22.62 | 1200. | ||
23.06 | 1300. | ||
23.40 | 1400. | ||
23.67 | 1500. |
Reaction thermochemistry data
Go To: Top, Gas phase thermochemistry data, Gas phase ion energetics data, Ion clustering data, Gas Chromatography, 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
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- + CH2O2 = (Cl- • CH2O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 27.4 ± 2.0 | kcal/mol | TDAs | French, Ikuta, et al., 1982 | gas phase; B,M |
ΔrH° | 27.7 ± 2.1 | kcal/mol | CIDT | Walker and Sunderlin, 1999 | gas phase; B |
ΔrH° | 25.6 ± 2.0 | kcal/mol | IMRE | Larson and McMahon, 1984 | gas phase; B,M |
ΔrH° | 37.2 ± 2.0 | kcal/mol | TDAs | Yamdagni and Kebarle, 1971 | gas phase; In serious disagreement with other's values. Source of error not obvious.; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 24.5 | cal/mol*K | PHPMS | French, Ikuta, et al., 1982 | gas phase; M |
ΔrS° | 24.1 | cal/mol*K | N/A | Larson and McMahon, 1984, 2 | gas phase; switching reaction(Cl-)t-C4H9OH, Entropy change calculated or estimated; French, Ikuta, et al., 1982; M |
ΔrS° | 39.6 | cal/mol*K | PHPMS | Yamdagni and Kebarle, 1971 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 20.1 ± 2.0 | kcal/mol | TDAs | French, Ikuta, et al., 1982 | gas phase; B |
ΔrG° | 18.4 ± 2.0 | kcal/mol | IMRE | Larson and McMahon, 1984 | gas phase; B,M |
ΔrG° | 25.4 ± 2.0 | kcal/mol | TDAs | Yamdagni and Kebarle, 1971 | gas phase; In serious disagreement with other's values. Source of error not obvious.; B |
By formula: CHO2- + H+ = CH2O2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 346.2 ± 1.2 | kcal/mol | D-EA | Kim, Bradforth, et al., 1995 | gas phase; dHacid(0K) = 344.67±0.62 kcal/mol; B |
ΔrH° | 345.3 ± 2.2 | kcal/mol | G+TS | Caldwell, Renneboog, et al., 1989 | gas phase; B |
ΔrH° | 345.4 ± 2.2 | kcal/mol | G+TS | Fujio, McIver, et al., 1981 | gas phase; value altered from reference due to change in acidity scale; B |
ΔrH° | 345.2 ± 2.9 | kcal/mol | G+TS | Cumming and Kebarle, 1978 | gas phase; B |
ΔrH° | 340.1 ± 4.6 | kcal/mol | EIAE | Muftakhov, Vasil'ev, et al., 1999 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 339.2 ± 1.5 | kcal/mol | H-TS | Kim, Bradforth, et al., 1995 | gas phase; dHacid(0K) = 344.67±0.62 kcal/mol; B |
ΔrG° | 338.3 ± 2.0 | kcal/mol | IMRE | Caldwell, Renneboog, et al., 1989 | gas phase; B |
ΔrG° | 338.4 ± 2.0 | kcal/mol | IMRE | Fujio, McIver, et al., 1981 | gas phase; value altered from reference due to change in acidity scale; B |
ΔrG° | 338.2 ± 2.0 | kcal/mol | IMRE | Cumming and Kebarle, 1978 | gas phase; B |
By formula: F- + CH2O2 = (F- • CH2O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 45.3 ± 2.0 | kcal/mol | IMRE | Larson and McMahon, 1983 | gas phase; These relative affinities are ca. 10 kcal/mol weaker than threshold values (see Wenthold and Squires, 1995) for donors greater than ca. 27 kcal/mol in free energy. This discrepancy has not yet been resolved, though the stronger value appears preferable.; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 24.2 | cal/mol*K | N/A | Larson and McMahon, 1983 | gas phase; switching reaction(F-)H2O, Entropy change calculated or estimated; Arshadi, Yamdagni, et al., 1970; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 38.1 ± 2.0 | kcal/mol | IMRE | Larson and McMahon, 1983 | gas phase; These relative affinities are ca. 10 kcal/mol weaker than threshold values (see Wenthold and Squires, 1995) for donors greater than ca. 27 kcal/mol in free energy. This discrepancy has not yet been resolved, though the stronger value appears preferable.; B,M |
By formula: CH5O+ + CH2O2 = (CH5O+ • CH2O2)
Bond type: Hydrogen bonds of the type OH-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 32.0 | kcal/mol | ICR | Larson and McMahon, 1982 | gas phase; switching reaction((CH3)2OH+)(CH3)2O, Entropy change calculated or estimated; Grimsrud and Kebarle, 1973, Lias, Liebman, et al., 1984, Keesee and Castleman, 1986; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 27.7 | cal/mol*K | N/A | Larson and McMahon, 1982 | gas phase; switching reaction((CH3)2OH+)(CH3)2O, Entropy change calculated or estimated; Grimsrud and Kebarle, 1973, Lias, Liebman, et al., 1984, Keesee and Castleman, 1986; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 23.8 | kcal/mol | ICR | Larson and McMahon, 1982 | gas phase; switching reaction((CH3)2OH+)(CH3)2O, Entropy change calculated or estimated; Grimsrud and Kebarle, 1973, Lias, Liebman, et al., 1984, Keesee and Castleman, 1986; M |
By formula: I- + CH2O2 = (I- • CH2O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 18.9 ± 1.0 | kcal/mol | TDAs | Caldwell and Kebarle, 1984 | gas phase; B,M |
ΔrH° | 12.9 ± 2.1 | kcal/mol | CIDT | Walker and Sunderlin, 1999 | gas phase; Authors suggest real value somewhere between this and Caldwell and Kebarle, 1984; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 20.7 | cal/mol*K | PHPMS | Caldwell and Kebarle, 1984 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 12.7 ± 1.0 | kcal/mol | TDAs | Caldwell and Kebarle, 1984 | gas phase; B |
By formula: (Cl- • CH2O2) + CH2O2 = (Cl- • 2CH2O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 11.2 ± 2.1 | kcal/mol | CIDT | Walker and Sunderlin, 1999 | gas phase; B |
ΔrH° | 34.1 ± 3.1 | kcal/mol | N/A | Luczynski, Wlodek, et al., 1978 | gas phase; Buffer gas: H2. Value too bound based on French, Ikuta, et al., 1982, by Grimsrud fractionation factor ( Williamson, Knighton, et al., 1996).; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 55. | cal/mol*K | HPMS | Luczynski, Wlodek, et al., 1978 | gas phase; Entropy change is questionable; M |
By formula: (Cl- • 4CH2O2) + CH2O2 = (Cl- • 5CH2O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 10.1 ± 2.0 | kcal/mol | N/A | Luczynski, Wlodek, et al., 1978 | gas phase; Buffer gas: H2. Value too bound based on French, Ikuta, et al., 1982, by Grimsrud fractionation factor ( Williamson, Knighton, et al., 1996).; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 11.5 | cal/mol*K | HPMS | Luczynski, Wlodek, et al., 1978 | gas phase; Entropy change is questionable; M |
By formula: (Cl- • 2CH2O2) + CH2O2 = (Cl- • 3CH2O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 22.2 ± 2.7 | kcal/mol | N/A | Luczynski, Wlodek, et al., 1978 | gas phase; Buffer gas: H2. Value too bound based on French, Ikuta, et al., 1982, by Grimsrud fractionation factor ( Williamson, Knighton, et al., 1996).; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 35. | cal/mol*K | HPMS | Luczynski, Wlodek, et al., 1978 | gas phase; Entropy change is questionable; M |
By formula: CHO2- + CH2O2 = (CHO2- • CH2O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 36.8 ± 1.0 | kcal/mol | N/A | Meot-Ner and Sieck, 1986 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 39.1 | cal/mol*K | PHPMS | Meot-Ner and Sieck, 1986 | gas phase; large ΔrH, ΔrS,; cyclic structure? pyrolysis?; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 25.1 ± 1.6 | kcal/mol | TDAs | Meot-Ner and Sieck, 1986 | gas phase; B |
By formula: (CHO2- • 4CH2O2) + CH2O2 = (CHO2- • 5CH2O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 10.1 ± 2.0 | kcal/mol | N/A | Luczynski, Wlodek, et al., 1978 | gas phase; Buffer gas H2. There may be appreciable fractionation of neutral gases: Williamson, Knighton, et al., 1996; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 12. | cal/mol*K | HPMS | Luczynski, Wlodek, et al., 1978 | gas phase; Entropy change is questionable; M |
By formula: (Cl- • 3CH2O2) + CH2O2 = (Cl- • 4CH2O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 14.1 ± 2.2 | kcal/mol | N/A | Luczynski, Wlodek, et al., 1978 | gas phase; Buffer gas: H2. Value too bound based on French, Ikuta, et al., 1982, by Grimsrud fractionation factor ( Williamson, Knighton, et al., 1996).; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 20. | cal/mol*K | HPMS | Luczynski, Wlodek, et al., 1978 | gas phase; M |
By formula: (CHO2- • 3CH2O2) + CH2O2 = (CHO2- • 4CH2O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 14.2 ± 2.1 | kcal/mol | N/A | Luczynski, Wlodek, et al., 1978 | gas phase; Buffer gas H2. There may be appreciable fractionation of neutral gases: Williamson, Knighton, et al., 1996; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 21.5 | cal/mol*K | HPMS | Luczynski, Wlodek, et al., 1978 | gas phase; M |
By formula: (CHO2- • 2CH2O2) + CH2O2 = (CHO2- • 3CH2O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 20.0 ± 2.6 | kcal/mol | N/A | Luczynski, Wlodek, et al., 1978 | gas phase; Buffer gas H2. There may be appreciable fractionation of neutral gases: Williamson, Knighton, et al., 1996; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 30. | cal/mol*K | HPMS | Luczynski, Wlodek, et al., 1978 | gas phase; M |
By formula: (CHO2- • CH2O2) + CH2O2 = (CHO2- • 2CH2O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 26.1 ± 3.1 | kcal/mol | N/A | Luczynski, Wlodek, et al., 1978 | gas phase; Buffer gas H2. There may be appreciable fractionation of neutral gases: Williamson, Knighton, et al., 1996; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 34. | cal/mol*K | HPMS | Luczynski, Wlodek, et al., 1978 | gas phase; M |
By formula: CH6N+ + CH2O2 = (CH6N+ • CH2O2)
Bond type: Hydrogen bonds of the type NH+-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 19.0 | kcal/mol | PHPMS | Meot-Ner, 1984 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 24.2 | cal/mol*K | PHPMS | Meot-Ner, 1984 | gas phase; M |
By formula: CH2NO5- + H2O + CH2O2 = CH4NO6-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrG° | 4.40 ± 0.20 | kcal/mol | IMRE | Viidanoja, Reiner, et al., 2000 | gas phase; B |
+ = CH2BrO2-
By formula: Br- + CH2O2 = CH2BrO2-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 17.2 ± 1.7 | kcal/mol | CIDT | Walker and Sunderlin, 1999 | gas phase; B |
By formula: CH2IO2- + 2CH2O2 = C2H4IO4-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 10.0 ± 2.1 | kcal/mol | CIDT | Walker and Sunderlin, 1999 | gas phase; B |
+ = CH2NO5-
By formula: NO3- + CH2O2 = CH2NO5-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrG° | 11.40 ± 0.20 | kcal/mol | IMRE | Viidanoja, Reiner, et al., 1998 | gas phase; B |
By formula: CH2BrO2- + 2CH2O2 = C2H4BrO4-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 9.6 ± 1.7 | kcal/mol | CIDT | Walker and Sunderlin, 1999 | gas phase; B |
Gas phase ion energetics data
Go To: Top, Gas phase thermochemistry data, Reaction thermochemistry data, Ion clustering data, Gas Chromatography, 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
LL - Sharon G. Lias and Joel F. Liebman
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
IE (evaluated) | 11.33 ± 0.01 | eV | N/A | N/A | L |
Quantity | Value | Units | Method | Reference | Comment |
Proton affinity (review) | 177.3 | kcal/mol | N/A | Hunter and Lias, 1998 | HL |
Quantity | Value | Units | Method | Reference | Comment |
Gas basicity | 169.8 | kcal/mol | N/A | Hunter and Lias, 1998 | HL |
Ionization energy determinations
IE (eV) | Method | Reference | Comment |
---|---|---|---|
11.31 | PI | Traeger, 1985 | LBLHLM |
11.329 ± 0.002 | S | Bell, Ng, et al., 1975 | LLK |
11.16 ± 0.03 | PI | Warneck, 1974 | LLK |
11.314 ± 0.002 | PI | Knowles and Nicholson, 1974 | LLK |
11.3 | PE | Watanabe, Yokoyama, et al., 1973 | LLK |
11.33 | PE | Watanabe, Yokoyama, et al., 1973, 2 | LLK |
11.35 ± 0.03 | PE | Thomas, 1972 | LLK |
11.16 ± 0.03 | PI | Matthews and Warneck, 1969 | RDSH |
11.33 | PE | Brundle, Turner, et al., 1969 | RDSH |
11.05 ± 0.03 | PI | Vilesov, 1960 | RDSH |
11.05 ± 0.01 | PI | Watanabe, 1957 | RDSH |
11.33 | S | Price and Evans, 1937 | RDSH |
11.5 | PE | Von Niessen, Bieri, et al., 1980 | Vertical value; LLK |
11.34 | PE | Benoit and Harrison, 1977 | Vertical value; LLK |
10.7 | PE | Rao, 1975 | Vertical value; LLK |
11.51 | PE | Kimura, Katsumata, et al., 1975 | Vertical value; LLK |
Appearance energy determinations
Ion | AE (eV) | Other Products | Method | Reference | Comment |
---|---|---|---|---|---|
C+ | 22.7 ± 0.5 | O+H2O | EI | Stepanov, Perov, et al., 1988 | LL |
CHO+ | 12.76 | OH | PI | Traeger, 1985 | LBLHLM |
CHO+ | 13.0 ± 0.1 | OH | PI | Golovin, Akopyan, et al., 1979 | LLK |
CHO+ | 12.79 ± 0.03 | OH | PI | Warneck, 1974 | LLK |
CHO+ | 12.79 ± 0.03 | OH | PI | Matthews and Warneck, 1969 | RDSH |
CHO2+ | 12.4 ± 0.1 | H | PI | Golovin, Akopyan, et al., 1979 | LLK |
CHO2+ | 12.26 | H | PI | Akopyan and Villem, 1976 | LLK |
CHO2+ | 12.29 ± 0.03 | H | PI | Warneck, 1974 | LLK |
HO+ | 17.97 ± 0.06 | HCO | PI | Warneck, 1974 | LLK |
O+ | 20.0 ± 0.5 | CO+H2 | EI | Stepanov, Perov, et al., 1988 | LL |
De-protonation reactions
By formula: CHO2- + H+ = CH2O2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 346.2 ± 1.2 | kcal/mol | D-EA | Kim, Bradforth, et al., 1995 | gas phase; dHacid(0K) = 344.67±0.62 kcal/mol; B |
ΔrH° | 345.3 ± 2.2 | kcal/mol | G+TS | Caldwell, Renneboog, et al., 1989 | gas phase; B |
ΔrH° | 345.4 ± 2.2 | kcal/mol | G+TS | Fujio, McIver, et al., 1981 | gas phase; value altered from reference due to change in acidity scale; B |
ΔrH° | 345.2 ± 2.9 | kcal/mol | G+TS | Cumming and Kebarle, 1978 | gas phase; B |
ΔrH° | 340.1 ± 4.6 | kcal/mol | EIAE | Muftakhov, Vasil'ev, et al., 1999 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 339.2 ± 1.5 | kcal/mol | H-TS | Kim, Bradforth, et al., 1995 | gas phase; dHacid(0K) = 344.67±0.62 kcal/mol; B |
ΔrG° | 338.3 ± 2.0 | kcal/mol | IMRE | Caldwell, Renneboog, et al., 1989 | gas phase; B |
ΔrG° | 338.4 ± 2.0 | kcal/mol | IMRE | Fujio, McIver, et al., 1981 | gas phase; value altered from reference due to change in acidity scale; B |
ΔrG° | 338.2 ± 2.0 | kcal/mol | IMRE | Cumming and Kebarle, 1978 | gas phase; B |
Ion clustering data
Go To: Top, Gas phase thermochemistry data, Reaction thermochemistry data, Gas phase ion energetics data, Gas Chromatography, 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
Note: Please consider using the reaction search for this species. This page allows searching of all reactions involving this species. Searches may be limited to ion clustering reactions. A general reaction search form is also available.
Clustering reactions
+ = CH2BrO2-
By formula: Br- + CH2O2 = CH2BrO2-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 17.2 ± 1.7 | kcal/mol | CIDT | Walker and Sunderlin, 1999 | gas phase; B |
By formula: CHO2- + CH2O2 = (CHO2- • CH2O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 36.8 ± 1.0 | kcal/mol | N/A | Meot-Ner and Sieck, 1986 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 39.1 | cal/mol*K | PHPMS | Meot-Ner and Sieck, 1986 | gas phase; large ΔrH, ΔrS,; cyclic structure? pyrolysis?; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 25.1 ± 1.6 | kcal/mol | TDAs | Meot-Ner and Sieck, 1986 | gas phase; B |
By formula: (CHO2- • CH2O2) + CH2O2 = (CHO2- • 2CH2O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 26.1 ± 3.1 | kcal/mol | N/A | Luczynski, Wlodek, et al., 1978 | gas phase; Buffer gas H2. There may be appreciable fractionation of neutral gases: Williamson, Knighton, et al., 1996; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 34. | cal/mol*K | HPMS | Luczynski, Wlodek, et al., 1978 | gas phase; M |
By formula: (CHO2- • 2CH2O2) + CH2O2 = (CHO2- • 3CH2O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 20.0 ± 2.6 | kcal/mol | N/A | Luczynski, Wlodek, et al., 1978 | gas phase; Buffer gas H2. There may be appreciable fractionation of neutral gases: Williamson, Knighton, et al., 1996; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 30. | cal/mol*K | HPMS | Luczynski, Wlodek, et al., 1978 | gas phase; M |
By formula: (CHO2- • 3CH2O2) + CH2O2 = (CHO2- • 4CH2O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 14.2 ± 2.1 | kcal/mol | N/A | Luczynski, Wlodek, et al., 1978 | gas phase; Buffer gas H2. There may be appreciable fractionation of neutral gases: Williamson, Knighton, et al., 1996; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 21.5 | cal/mol*K | HPMS | Luczynski, Wlodek, et al., 1978 | gas phase; M |
By formula: (CHO2- • 4CH2O2) + CH2O2 = (CHO2- • 5CH2O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 10.1 ± 2.0 | kcal/mol | N/A | Luczynski, Wlodek, et al., 1978 | gas phase; Buffer gas H2. There may be appreciable fractionation of neutral gases: Williamson, Knighton, et al., 1996; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 12. | cal/mol*K | HPMS | Luczynski, Wlodek, et al., 1978 | gas phase; Entropy change is questionable; M |
By formula: CH2BrO2- + 2CH2O2 = C2H4BrO4-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 9.6 ± 1.7 | kcal/mol | CIDT | Walker and Sunderlin, 1999 | gas phase; B |
By formula: CH2IO2- + 2CH2O2 = C2H4IO4-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 10.0 ± 2.1 | kcal/mol | CIDT | Walker and Sunderlin, 1999 | gas phase; B |
By formula: CH2NO5- + H2O + CH2O2 = CH4NO6-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrG° | 4.40 ± 0.20 | kcal/mol | IMRE | Viidanoja, Reiner, et al., 2000 | gas phase; B |
By formula: CH5O+ + CH2O2 = (CH5O+ • CH2O2)
Bond type: Hydrogen bonds of the type OH-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 32.0 | kcal/mol | ICR | Larson and McMahon, 1982 | gas phase; switching reaction((CH3)2OH+)(CH3)2O, Entropy change calculated or estimated; Grimsrud and Kebarle, 1973, Lias, Liebman, et al., 1984, Keesee and Castleman, 1986; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 27.7 | cal/mol*K | N/A | Larson and McMahon, 1982 | gas phase; switching reaction((CH3)2OH+)(CH3)2O, Entropy change calculated or estimated; Grimsrud and Kebarle, 1973, Lias, Liebman, et al., 1984, Keesee and Castleman, 1986; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 23.8 | kcal/mol | ICR | Larson and McMahon, 1982 | gas phase; switching reaction((CH3)2OH+)(CH3)2O, Entropy change calculated or estimated; Grimsrud and Kebarle, 1973, Lias, Liebman, et al., 1984, Keesee and Castleman, 1986; M |
By formula: CH6N+ + CH2O2 = (CH6N+ • CH2O2)
Bond type: Hydrogen bonds of the type NH+-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 19.0 | kcal/mol | PHPMS | Meot-Ner, 1984 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 24.2 | cal/mol*K | PHPMS | Meot-Ner, 1984 | gas phase; M |
By formula: Cl- + CH2O2 = (Cl- • CH2O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 27.4 ± 2.0 | kcal/mol | TDAs | French, Ikuta, et al., 1982 | gas phase; B,M |
ΔrH° | 27.7 ± 2.1 | kcal/mol | CIDT | Walker and Sunderlin, 1999 | gas phase; B |
ΔrH° | 25.6 ± 2.0 | kcal/mol | IMRE | Larson and McMahon, 1984 | gas phase; B,M |
ΔrH° | 37.2 ± 2.0 | kcal/mol | TDAs | Yamdagni and Kebarle, 1971 | gas phase; In serious disagreement with other's values. Source of error not obvious.; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 24.5 | cal/mol*K | PHPMS | French, Ikuta, et al., 1982 | gas phase; M |
ΔrS° | 24.1 | cal/mol*K | N/A | Larson and McMahon, 1984, 2 | gas phase; switching reaction(Cl-)t-C4H9OH, Entropy change calculated or estimated; French, Ikuta, et al., 1982; M |
ΔrS° | 39.6 | cal/mol*K | PHPMS | Yamdagni and Kebarle, 1971 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 20.1 ± 2.0 | kcal/mol | TDAs | French, Ikuta, et al., 1982 | gas phase; B |
ΔrG° | 18.4 ± 2.0 | kcal/mol | IMRE | Larson and McMahon, 1984 | gas phase; B,M |
ΔrG° | 25.4 ± 2.0 | kcal/mol | TDAs | Yamdagni and Kebarle, 1971 | gas phase; In serious disagreement with other's values. Source of error not obvious.; B |
By formula: (Cl- • CH2O2) + CH2O2 = (Cl- • 2CH2O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 11.2 ± 2.1 | kcal/mol | CIDT | Walker and Sunderlin, 1999 | gas phase; B |
ΔrH° | 34.1 ± 3.1 | kcal/mol | N/A | Luczynski, Wlodek, et al., 1978 | gas phase; Buffer gas: H2. Value too bound based on French, Ikuta, et al., 1982, by Grimsrud fractionation factor ( Williamson, Knighton, et al., 1996).; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 55. | cal/mol*K | HPMS | Luczynski, Wlodek, et al., 1978 | gas phase; Entropy change is questionable; M |
By formula: (Cl- • 2CH2O2) + CH2O2 = (Cl- • 3CH2O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 22.2 ± 2.7 | kcal/mol | N/A | Luczynski, Wlodek, et al., 1978 | gas phase; Buffer gas: H2. Value too bound based on French, Ikuta, et al., 1982, by Grimsrud fractionation factor ( Williamson, Knighton, et al., 1996).; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 35. | cal/mol*K | HPMS | Luczynski, Wlodek, et al., 1978 | gas phase; Entropy change is questionable; M |
By formula: (Cl- • 3CH2O2) + CH2O2 = (Cl- • 4CH2O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 14.1 ± 2.2 | kcal/mol | N/A | Luczynski, Wlodek, et al., 1978 | gas phase; Buffer gas: H2. Value too bound based on French, Ikuta, et al., 1982, by Grimsrud fractionation factor ( Williamson, Knighton, et al., 1996).; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 20. | cal/mol*K | HPMS | Luczynski, Wlodek, et al., 1978 | gas phase; M |
By formula: (Cl- • 4CH2O2) + CH2O2 = (Cl- • 5CH2O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 10.1 ± 2.0 | kcal/mol | N/A | Luczynski, Wlodek, et al., 1978 | gas phase; Buffer gas: H2. Value too bound based on French, Ikuta, et al., 1982, by Grimsrud fractionation factor ( Williamson, Knighton, et al., 1996).; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 11.5 | cal/mol*K | HPMS | Luczynski, Wlodek, et al., 1978 | gas phase; Entropy change is questionable; M |
By formula: F- + CH2O2 = (F- • CH2O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 45.3 ± 2.0 | kcal/mol | IMRE | Larson and McMahon, 1983 | gas phase; These relative affinities are ca. 10 kcal/mol weaker than threshold values (see Wenthold and Squires, 1995) for donors greater than ca. 27 kcal/mol in free energy. This discrepancy has not yet been resolved, though the stronger value appears preferable.; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 24.2 | cal/mol*K | N/A | Larson and McMahon, 1983 | gas phase; switching reaction(F-)H2O, Entropy change calculated or estimated; Arshadi, Yamdagni, et al., 1970; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 38.1 ± 2.0 | kcal/mol | IMRE | Larson and McMahon, 1983 | gas phase; These relative affinities are ca. 10 kcal/mol weaker than threshold values (see Wenthold and Squires, 1995) for donors greater than ca. 27 kcal/mol in free energy. This discrepancy has not yet been resolved, though the stronger value appears preferable.; B,M |
By formula: I- + CH2O2 = (I- • CH2O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 18.9 ± 1.0 | kcal/mol | TDAs | Caldwell and Kebarle, 1984 | gas phase; B,M |
ΔrH° | 12.9 ± 2.1 | kcal/mol | CIDT | Walker and Sunderlin, 1999 | gas phase; Authors suggest real value somewhere between this and Caldwell and Kebarle, 1984; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 20.7 | cal/mol*K | PHPMS | Caldwell and Kebarle, 1984 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 12.7 ± 1.0 | kcal/mol | TDAs | Caldwell and Kebarle, 1984 | gas phase; B |
+ = CH2NO5-
By formula: NO3- + CH2O2 = CH2NO5-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrG° | 11.40 ± 0.20 | kcal/mol | IMRE | Viidanoja, Reiner, et al., 1998 | gas phase; B |
Gas Chromatography
Go To: Top, Gas phase thermochemistry data, Reaction thermochemistry data, Gas phase ion energetics data, Ion clustering 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: NIST Mass Spectrometry Data Center, William E. Wallace, director
Van Den Dool and Kratz RI, non-polar column, temperature ramp
Column type | Active phase | I | Reference | Comment |
---|---|---|---|---|
Capillary | DB-1 | 543. | Helmig, Pollock, et al., 1996 | 30. m/0.25 mm/1. μm, 6. K/min; Tstart: -50. C; Tend: 180. C |
Van Den Dool and Kratz RI, non-polar column, custom temperature program
Column type | Active phase | I | Reference | Comment |
---|---|---|---|---|
Capillary | Methyl Silicone | 512. | Peng, Yang, et al., 1991 | Program: not specified |
Packed | SE-30 | 512. | Peng, Ding, et al., 1988 | Supelcoport; Chromosorb; Column length: 3.05 m; Program: 40C(5min) => 10C/min => 200C or 250C (60min) |
Van Den Dool and Kratz RI, polar column, temperature ramp
Column type | Active phase | I | Reference | Comment |
---|---|---|---|---|
Capillary | DB-Wax | 1510. | Mahajan, Goddik, et al., 2004 | 30. m/0.25 mm/0.5 μm, He, 40. C @ 2. min, 5. K/min, 230. C @ 10. min |
Van Den Dool and Kratz RI, polar column, custom temperature program
Column type | Active phase | I | Reference | Comment |
---|---|---|---|---|
Capillary | Stabilwax | 1528. | Natali N., Chinnici F., et al., 2006 | 30. m/0.25 mm/0.25 μm, He; Program: 40C => 3C/min => 100C => 5C/min => 240C(10min) |
Capillary | DB-Wax | 1543.6 | Yang, Chyau, et al., 1998 | He; Column length: 50. m; Column diameter: 0.32 mm; Program: 50C => 2.5C/min => 150C => 1.5C/min => 210C |
Normal alkane RI, non-polar column, temperature ramp
Column type | Active phase | I | Reference | Comment |
---|---|---|---|---|
Capillary | HP-1 | 495. | Castel, Fernandez, et al., 2006 | 50. m/0.2 mm/0.33 μm, He, 60. C @ 4. min, 2. K/min, 250. C @ 30. min |
Normal alkane RI, non-polar column, custom temperature program
Column type | Active phase | I | Reference | Comment |
---|---|---|---|---|
Capillary | Methyl Silicone | 490. | Zenkevich, Korolenko, et al., 1995 | Program: not specified |
Normal alkane RI, polar column, temperature ramp
Column type | Active phase | I | Reference | Comment |
---|---|---|---|---|
Capillary | DB-Wax | 1470. | Guo, Wu, et al., 2008 | 30. m/0.25 mm/0.25 μm, Helium, 60. C @ 2. min, 10. K/min, 250. C @ 10. min |
Capillary | DB-Wax | 1470. | Guo, Wu, et al., 2008 | 30. m/0.25 mm/0.25 μm, Helium, 60. C @ 2. min, 10. K/min, 250. C @ 10. min |
Capillary | DB-Wax | 1470. | Guo, Wu, et al., 2008 | 30. m/0.25 mm/0.25 μm, Helium, 60. C @ 2. min, 10. K/min, 250. C @ 10. min |
Capillary | RTX-Wax | 1485. | Prososki, Etzel, et al., 2007 | 30. m/0.25 mm/0.5 μm, He, 40. C @ 5. min, 10. K/min, 220. C @ 10. min |
Capillary | Supelcowax-10 | 1521. | Vichi, Castellote, et al., 2003 | 30. m/0.25 mm/0.25 μm, He, 40. C @ 10. min, 3. K/min; Tend: 200. C |
Capillary | DB-Wax | 1492. | Sekiwa, Kubota, et al., 1997 | He, 2. K/min; Column length: 60. m; Column diameter: 0.25 mm; Tstart: 60. C; Tend: 180. C |
Capillary | DB-Wax | 1499. | Umano, Hagi, et al., 1995 | He, 40. C @ 2. min, 2. K/min; Column length: 60. m; Column diameter: 0.25 mm; Tend: 200. C |
Capillary | FFAP | 1505. | Vernin, Metzger, et al., 1988 | He, 60. C @ 5. min, 2. K/min; Column length: 50. m; Column diameter: 0.28 mm; Tend: 240. C |
Normal alkane RI, polar column, custom temperature program
Column type | Active phase | I | Reference | Comment |
---|---|---|---|---|
Capillary | DB-Wax | 1501. | Gonzalez-Rios, Suarez-Quiroz, et al., 2007 | 30. m/0.25 mm/0.25 μm, Hydrogen; Program: 44 0C 3 0C/min -> 170 0C 8 0C/min -> 250 0C |
Capillary | CP-Wax 52CB | 1532. | Muresan, Eillebrecht, et al., 2000 | 50. m/0.32 mm/1.2 μm; Program: 40C(10min) => 3C/min => 190C => 10C/min => 250C(5min) |
Capillary | Polyethylene Glycol | 1533. | Zenkevich, Korolenko, et al., 1995 | Program: not specified |
References
Go To: Top, Gas phase thermochemistry data, Reaction thermochemistry data, Gas phase ion energetics data, Ion clustering data, Gas Chromatography, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
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Notes
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- Symbols used in this document:
AE Appearance energy Cp,gas Constant pressure heat capacity of gas IE (evaluated) Recommended ionization energy S°gas Entropy of gas at standard conditions 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 - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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