Acetic acid
- Formula: C2H4O2
- Molecular weight: 60.0520
- IUPAC Standard InChIKey: QTBSBXVTEAMEQO-UHFFFAOYSA-N
- CAS Registry Number: 64-19-7
- 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. - Isotopologues:
- Other names: Ethanoic acid; Ethylic acid; Glacial acetic acid; Methanecarboxylic acid; Vinegar acid; CH3COOH; Acetasol; Acide acetique; Acido acetico; Azijnzuur; Essigsaeure; Octowy kwas; Acetic acid, glacial; Kyselina octova; UN 2789; Aci-jel; Shotgun; Ethanoic acid monomer; NSC 132953
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Gas phase thermochemistry data
Go To: Top, Phase change data, Henry's Law 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 as indicated in comments:
DRB - Donald R. Burgess, Jr.
GT - Glushko Thermocenter, Russian Academy of Sciences, Moscow
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°gas | -103.5 ± 0.6 | kcal/mol | AVG | N/A | Average of 8 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
S°gas | 67.600 | cal/mol*K | N/A | Weltner W., 1955 | Other third-law entropy values at 298.15 K are 284.5 [ Chao J., 1986] and 290.37(4.18) J/mol*K [ Halford J.O., 1941].; GT |
Constant pressure heat capacity of gas
Cp,gas (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
9.450 | 50. | Chao J., 1986 | p=1 bar. Selected entropies and heat capacities differ from other statistically calculated values [ Weltner W., 1955] by 1.0-1.3 J/mol*K for S(T) and 3.1-5.4 J/mol*K for Cp(T). Please also see Chao J., 1978.; GT |
9.661 | 100. | ||
10.22 | 150. | ||
11.55 | 200. | ||
14.19 | 273.15 | ||
15.16 ± 0.026 | 298.15 | ||
15.23 | 300. | ||
19.04 | 400. | ||
22.45 | 500. | ||
25.378 | 600. | ||
27.875 | 700. | ||
29.995 | 800. | ||
31.785 | 900. | ||
33.284 | 1000. | ||
34.527 | 1100. | ||
35.554 | 1200. | ||
36.401 | 1300. | ||
37.098 | 1400. | ||
37.674 | 1500. |
Phase change data
Go To: Top, Gas phase thermochemistry data, Henry's Law 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 as indicated in comments:
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, Chris Muzny director
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 | 391.2 ± 0.6 | K | AVG | N/A | Average of 80 out of 90 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 289.6 ± 0.5 | K | AVG | N/A | Average of 8 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 289.8 | K | N/A | Wilhoit, Chao, et al., 1985 | Uncertainty assigned by TRC = 0.05 K; TRC |
Ttriple | 289.69 | K | N/A | Martin and Andon, 1982 | Uncertainty assigned by TRC = 0.04 K; TRC |
Ttriple | 289.8 | K | N/A | Parks and Kelley, 1925 | Uncertainty assigned by TRC = 0.15 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 593. ± 3. | K | AVG | N/A | Average of 10 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 57.05 | atm | N/A | Andereya and Chase, 1990 | Uncertainty assigned by TRC = 0.20 atm; TRC |
Pc | 57.5279 | atm | N/A | D'Souza and Teja, 1987 | Uncertainty assigned by TRC = 0.89 atm; Ambrose's procedure; TRC |
Pc | 57.10 | atm | N/A | Ambrose, Ellender, et al., 1977 | Uncertainty assigned by TRC = 0.08 atm; TRC |
Pc | 57.11 | atm | N/A | Young, 1910 | Uncertainty assigned by TRC = 0.99995 atm; TRC |
Pc | 57.110 | atm | N/A | Young, 1891 | Uncertainty assigned by TRC = 0.2631 atm; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 5.84 | mol/l | N/A | Vandana and Teja, 1995 | Uncertainty assigned by TRC = 0.02 mol/l; TRC |
ρc | 5.838 | mol/l | N/A | Young, 1910 | Uncertainty assigned by TRC = 0.02 mol/l; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 12.0 | kcal/mol | CGC | Verevkin, 2000 | Based on data from 303. to 378. K.; AC |
ΔvapH° | 12.3 | kcal/mol | N/A | Majer and Svoboda, 1985 | |
ΔvapH° | 12.3 ± 0.36 | kcal/mol | C | Konicek and Wadso, 1970 | ALS |
ΔvapH° | 12.3 ± 0.38 | kcal/mol | C | Konicek, Wadsö, et al., 1970 | AC |
Enthalpy of vaporization
ΔvapH (kcal/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
5.66 | 391.1 | N/A | Majer and Svoboda, 1985 | |
9.35 | 360. | EB | Muñoz and Krähenbühl, 2001 | Based on data from 345. to 383. K.; AC |
9.78 | 335. | N/A | Vercher, Vázquez, et al., 2001 | Based on data from 320. to 395. K.; AC |
9.06 | 406. | A | Stephenson and Malanowski, 1987 | Based on data from 391. to 550. K.; AC |
10.0 | 305. | A | Stephenson and Malanowski, 1987 | Based on data from 290. to 396. K.; AC |
9.25 | 406. | A | Stephenson and Malanowski, 1987 | Based on data from 391. to 447. K.; AC |
9.11 | 452. | A | Stephenson and Malanowski, 1987 | Based on data from 437. to 535. K.; AC |
9.27 | 540. | A | Stephenson and Malanowski, 1987 | Based on data from 525. to 593. K.; AC |
9.94 | 304. | A | Stephenson and Malanowski, 1987 | Based on data from 289. to 392. K. See also Dykyj, 1970.; AC |
10.3 | 308. | N/A | Tamir, Dragoescu, et al., 1983 | AC |
9.63 | 340. | N/A | McDonald, Shrader, et al., 1959 | Based on data from 325. to 391. K.; AC |
9.94 | 318. | MM | Potter and Ritter, 1954 | Based on data from 303. to 399. K.; AC |
Enthalpy of vaporization
ΔvapH = A exp(-αTr)
(1 − Tr)β
ΔvapH =
Enthalpy of vaporization (at saturation pressure)
(kcal/mol)
Tr = reduced temperature (T / Tc)
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Temperature (K) | 298. to 392. |
---|---|
A (kcal/mol) | 5.459 |
α | 0.0184 |
β | -0.0454 |
Tc (K) | 592.7 |
Reference | Majer and Svoboda, 1985 |
Antoine Equation Parameters
log10(P) = A − (B / (T + C))
P = vapor pressure (atm)
T = temperature (K)
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Temperature (K) | A | B | C | Reference |
---|---|---|---|---|
290.26 to 391.01 | 4.67635 | 1642.54 | -39.764 | McDonald, Shrader, et al., 1959 |
Enthalpy of sublimation
ΔsubH (kcal/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
16.1 ± 0.2 | 223. | TE,ME | Calis-Van Ginkel, Calis, et al., 1978 | Based on data from 213. to 230. K.; AC |
17. ± 0.2 | 213. | TE,ME | Calis-Van Ginkel, Calis, et al., 1978 | Based on data from 213. to 230. K.; AC |
Enthalpy of fusion
ΔfusH (kcal/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
2.801 | 298.7 | Domalski and Hearing, 1996 | See also Martin and Andon, 1982, 2.; AC |
2.8031 | 289.9 | Parks and Kelley, 1925, 2 | DH |
2.588 | 289.8 | Louguinine and Dupont, 1911 | AC |
2.753 | 283.7 | Meyer, 1910 | AC |
2.6592 | 290.06 | Pickering, 1895 | DH |
Entropy of fusion
ΔfusS (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
9.673 | 289.9 | Parks and Kelley, 1925, 2 | DH |
9.168 | 290.06 | Pickering, 1895 | DH |
Enthalpy of phase transition
ΔHtrs (kcal/mol) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
2.8011 | 298.69 | crystaline, I | liquid | Martin and Andon, 1982, 2 | DH |
Entropy of phase transition
ΔStrs (cal/mol*K) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
9.68 | 298.69 | crystaline, I | liquid | Martin and Andon, 1982, 2 | DH |
Henry's Law data
Go To: Top, Gas phase thermochemistry data, Phase change 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: 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 |
---|---|---|---|---|
4100. | 6300. | M | N/A | |
5200. | C | N/A | ||
5400. | 6300. | Q | N/A | |
5200. | C | N/A | ||
8600. | C | N/A | ||
5500. | M | N/A | ||
820. | Q | N/A | missing citation give several references for the Henry's law constants but don't assign them to specific species. | |
9300. | M | N/A | The value given here was measured at a liquid phase volume mixing ratio of 1 ppmv. missing citation found that the Henry's law constant changes at higher concentrations. | |
8800. | 6400. | T | N/A | |
6400. | T | N/A | ||
8800. | T | N/A | ||
10000. | X | N/A | Value given here as quoted by missing citation. | |
970. | 4900. | X | N/A | |
3300. | Q | N/A | ||
3400. | c | N/A |
Gas phase ion energetics data
Go To: Top, Gas phase thermochemistry data, Phase change data, Henry's Law 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 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
View reactions leading to C2H4O2+ (ion structure unspecified)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
IE (evaluated) | 10.65 ± 0.02 | eV | N/A | N/A | L |
Quantity | Value | Units | Method | Reference | Comment |
Proton affinity (review) | 187.3 | kcal/mol | N/A | Hunter and Lias, 1998 | HL |
Quantity | Value | Units | Method | Reference | Comment |
Gas basicity | 179.9 | kcal/mol | N/A | Hunter and Lias, 1998 | HL |
Ionization energy determinations
IE (eV) | Method | Reference | Comment |
---|---|---|---|
10.63 | PI | Traeger, McLouglin, et al., 1982 | LBLHLM |
10.66 | EI | Holmes, Fingas, et al., 1981 | LLK |
10.66 ± 0.05 | EI | Holmes and Lossing, 1980 | LLK |
10.66 | EI | Holmes and Lossing, 1980, 2 | LLK |
10.66 ± 0.05 | PI | Akopyan and Villem, 1976 | LLK |
10.664 ± 0.003 | PI | Watanabe, Yokoyama, et al., 1974 | LLK |
10.644 ± 0.002 | PI | Knowles and Nicholson, 1974 | LLK |
10.65 | PE | Watanabe, Yokoyama, et al., 1973 | LLK |
10.69 ± 0.03 | PE | Thomas, 1972 | LLK |
10.70 | PE | Sweigart and Turner, 1972 | LLK |
10.37 ± 0.03 | PI | Watanabe, Nakayama, et al., 1962 | RDSH |
10.38 ± 0.03 | PI | Vilesov, 1960 | RDSH |
10.35 ± 0.03 | PI | Watanabe, 1957 | RDSH |
10.9 | PE | Von Niessen, Bieri, et al., 1980 | Vertical value; LLK |
10.84 | PE | Carnovale, Gan, et al., 1980 | Vertical value; LLK |
10.63 | PE | Benoit and Harrison, 1977 | Vertical value; LLK |
11.5 | PE | Rao, 1975 | Vertical value; LLK |
10.87 | PE | Kimura, Katsumata, et al., 1975 | Vertical value; LLK |
10.8 | PE | Green and Hayes, 1975 | Vertical value; LLK |
Appearance energy determinations
Ion | AE (eV) | Other Products | Method | Reference | Comment |
---|---|---|---|---|---|
C+ | 22.0 ± 0.5 | H2+HCOOH | EI | Stepanov, Perov, et al., 1988 | LL |
CHO2+ | 12.27 ± 0.05 | CH3 | EI | Haney and Franklin, 1969 | RDSH |
CHO2+ | 12.9 ± 0.1 | CH3 | EI | Shigorin, Filyugina, et al., 1966 | RDSH |
CH3+ | 14.0 ± 0.15 | ? | EI | Haney and Franklin, 1969 | RDSH |
CH3O+ | 12.05 ± 0.10 | CHO | EI | Selim and Helal, 1981 | LLK |
CO+ | 15.3 ± 0.1 | CH3OH | EI | Shigorin, Filyugina, et al., 1966 | RDSH |
C2H3O+ | 11.54 | OH | PI | Traeger, McLouglin, et al., 1982 | LBLHLM |
C2H3O+ | 11.75 | OH | EI | Haney and Franklin, 1969 | RDSH |
C2H3O+ | 11.4 ± 0.15 | OH | EI | Shigorin, Filyugina, et al., 1966 | RDSH |
OH+ | 15.1 | ? | EI | Majer, Patrick, et al., 1961 | RDSH |
De-protonation reactions
By formula: C2H3O2- + H+ = C2H4O2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 348.2 ± 1.4 | kcal/mol | CIDC | Angel and Ervin, 2006 | gas phase; B |
ΔrH° | 348.1 ± 2.2 | kcal/mol | G+TS | Taft and Topsom, 1987 | gas phase; B |
ΔrH° | 348.6 ± 2.1 | kcal/mol | G+TS | Cumming and Kebarle, 1978 | gas phase; B |
ΔrH° | 348.7 ± 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° | 343.20 ± 0.70 | kcal/mol | EIAE | Muftakhov, Vasil'ev, et al., 1999 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 341.1 ± 2.0 | kcal/mol | IMRE | Taft and Topsom, 1987 | gas phase; B |
ΔrG° | 341.5 ± 2.0 | kcal/mol | IMRE | Cumming and Kebarle, 1978 | gas phase; B |
ΔrG° | 341.7 ± 2.0 | kcal/mol | IMRE | Fujio, McIver, et al., 1981 | gas phase; value altered from reference due to change in acidity scale; B |
C2H3O2- + =
By formula: C2H3O2- + H+ = C2H4O2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 368.0 ± 3.1 | kcal/mol | G+TS | Grabowski and Cheng, 1989 | gas phase; B |
ΔrH° | 367.8 ± 4.6 | kcal/mol | EIAE | Muftakhov, Vasil'ev, et al., 1999 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 361.2 ± 3.0 | kcal/mol | IMRB | Grabowski and Cheng, 1989 | gas phase; B |
Ion clustering data
Go To: Top, Gas phase thermochemistry data, 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:
M - Michael M. Meot-Ner (Mautner) and Sharon G. Lias
B - John E. Bartmess
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
By formula: CH6N+ + C2H4O2 = (CH6N+ • C2H4O2)
Bond type: Hydrogen bonds of the type NH+-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 22.0 | kcal/mol | PHPMS | Meot-Ner, 1984 | gas phase; M |
ΔrH° | 21.4 | kcal/mol | PHPMS | Meot-Ner, 1984 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 24.3 | cal/mol*K | PHPMS | Meot-Ner, 1984 | gas phase; M |
ΔrS° | 24. | cal/mol*K | N/A | Meot-Ner, 1984 | gas phase; Entropy change calculated or estimated; M |
Free energy of reaction
ΔrG° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
10.3 | 459. | PHPMS | Meot-Ner, 1984 | gas phase; Entropy change calculated or estimated; M |
By formula: CO3- + C2H4O2 = C3H4O5-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrG° | 11.30 ± 0.20 | kcal/mol | IMRE | Viidanoja, Reiner, et al., 1998 | gas phase; B |
By formula: C2H3O2- + C2H4O2 = (C2H3O2- • C2H4O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 29.3 | kcal/mol | PHPMS | Meot-Ner and Sieck, 1986 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 29.6 | cal/mol*K | PHPMS | Meot-Ner and Sieck, 1986 | gas phase; M |
By formula: (C2H3O2- • C2H4O2) + C2H4O2 = (C2H3O2- • 2C2H4O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 19.6 | kcal/mol | PHPMS | Meot-Ner and Sieck, 1986 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 28.6 | cal/mol*K | PHPMS | Meot-Ner and Sieck, 1986 | gas phase; M |
By formula: (C2H3O2- • 2C2H4O2) + C2H4O2 = (C2H3O2- • 3C2H4O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 16.2 | kcal/mol | PHPMS | Meot-Ner and Sieck, 1986 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 33.2 | cal/mol*K | PHPMS | Meot-Ner and Sieck, 1986 | gas phase; M |
By formula: (C2H3O2- • C2H4O2 • H2O) + C2H4O2 = (C2H3O2- • 2C2H4O2 • H2O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 19.69 ± 0.50 | kcal/mol | N/A | Meot-ner, Elmore, et al., 1999 | gas phase; B |
ΔrH° | 16.2 ± 1.0 | kcal/mol | TDAs | Meot-Ner and Sieck, 1986 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 10.81 | kcal/mol | TDAs | Meot-ner, Elmore, et al., 1999 | gas phase; B |
ΔrG° | 6.2 ± 1.0 | kcal/mol | TDAs | Meot-Ner and Sieck, 1986 | gas phase; B |
By formula: (C2H3O2- • 2C2H4O2 • H2O) + C2H4O2 = (C2H3O2- • 3C2H4O2 • H2O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 12.50 ± 0.60 | kcal/mol | N/A | Meot-ner, Elmore, et al., 1999 | gas phase; B |
ΔrH° | 16.2 ± 1.0 | kcal/mol | TDAs | Meot-Ner and Sieck, 1986 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 5.73 | kcal/mol | TDAs | Meot-ner, Elmore, et al., 1999 | gas phase; B |
ΔrG° | 6.2 ± 1.0 | kcal/mol | TDAs | Meot-Ner and Sieck, 1986 | gas phase; B |
By formula: (C2H3O2- • H2O) + C2H4O2 = (C2H3O2- • C2H4O2 • H2O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 29.3 ± 1.0 | kcal/mol | TDAs | Meot-Ner and Sieck, 1986 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 20.4 ± 1.6 | kcal/mol | TDAs | Meot-Ner and Sieck, 1986 | gas phase; B |
By formula: C2H4NO5- + H2O + C2H4O2 = C2H6NO6-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrG° | 4.60 ± 0.20 | kcal/mol | IMRE | Viidanoja, Reiner, et al., 2000 | gas phase; B |
By formula: C2H5O+ + C2H4O2 = (C2H5O+ • C2H4O2)
Bond type: Hydrogen bonds of the type OH-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 28.1 | kcal/mol | PHPMS | Meot-Ner (Mautner), 1992 | gas phase; M |
ΔrH° | 29.5 | 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° | 28.3 | cal/mol*K | PHPMS | Meot-Ner (Mautner), 1992 | gas phase; M |
ΔrS° | 27.9 | 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° | 21.2 | 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: (C2H5O+ • C2H4O2) + C2H4O2 = (C2H5O+ • 2C2H4O2)
Bond type: Hydrogen bonds of the type OH-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 18.5 | kcal/mol | PHPMS | Meot-Ner (Mautner), 1992 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 24.5 | cal/mol*K | PHPMS | Meot-Ner (Mautner), 1992 | gas phase; M |
By formula: (C2H5O+ • 2C2H4O2) + C2H4O2 = (C2H5O+ • 3C2H4O2)
Bond type: Hydrogen bonds of the type OH-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 13.1 | kcal/mol | PHPMS | Meot-Ner (Mautner), 1992 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 22.4 | cal/mol*K | PHPMS | Meot-Ner (Mautner), 1992 | gas phase; M |
By formula: (C2H5O+ • 3C2H4O2) + C2H4O2 = (C2H5O+ • 4C2H4O2)
Bond type: Hydrogen bonds of the type OH-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 12. | kcal/mol | PHPMS | Meot-Ner (Mautner), 1992 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 25. | cal/mol*K | N/A | Meot-Ner (Mautner), 1992 | gas phase; Entropy change calculated or estimated; M |
Free energy of reaction
ΔrG° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
6.2 | 245. | PHPMS | Meot-Ner (Mautner), 1992 | gas phase; Entropy change calculated or estimated; M |
By formula: C2H7O+ + C2H4O2 = (C2H7O+ • C2H4O2)
Bond type: Hydrogen bonds of the type OH-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 29.3 | 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° | 28.4 | 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° | 20.8 | 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: C3H4O5- + H2O + C2H4O2 = C3H6O6-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrG° | 4.60 ± 0.20 | kcal/mol | IMRE | Viidanoja, Reiner, et al., 2000 | gas phase; B |
By formula: C4H10NO+ + C2H4O2 = (C4H10NO+ • C2H4O2)
Bond type: Hydrogen bonds of the type OH-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 18.4 | kcal/mol | PHPMS | Meot-Ner, 1984, 2 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 24.7 | cal/mol*K | PHPMS | Meot-Ner, 1984, 2 | gas phase; M |
By formula: C6H5NO2- + C2H4O2 = (C6H5NO2- • C2H4O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 22.60 ± 0.10 | kcal/mol | TDAs | Sieck, 1985 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 26.8 | cal/mol*K | PHPMS | Sieck, 1985 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 14.60 ± 0.20 | kcal/mol | TDAs | Sieck, 1985 | gas phase; B |
By formula: C6H5O- + C2H4O2 = (C6H5O- • C2H4O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 27.4 | kcal/mol | PHPMS | Meot-Ner and Sieck, 1986 | gas phase; calculated from CH3COO-.C6H5OH; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 24.0 | cal/mol*K | PHPMS | Meot-Ner and Sieck, 1986 | gas phase; calculated from CH3COO-.C6H5OH; M |
By formula: C6H5S- + C2H4O2 = (C6H5S- • C2H4O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 20.3 | kcal/mol | PHPMS | Sieck and Meot-ner, 1989 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 26.2 | cal/mol*K | PHPMS | Sieck and Meot-ner, 1989 | gas phase; M |
+ = C8H9O2S-
By formula: C6H5S- + C2H4O2 = C8H9O2S-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 20.30 ± 0.10 | kcal/mol | TDAs | Sieck and Meot-ner, 1989 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 12.50 ± 0.40 | kcal/mol | TDAs | Sieck and Meot-ner, 1989 | gas phase; B |
By formula: C6H12NO3+ + C2H4O2 = (C6H12NO3+ • C2H4O2)
Bond type: Hydrogen bonds with polydentate bonding in positive ions
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 18.1 | kcal/mol | PHPMS | Meot-Ner, 1984, 2 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 27.2 | cal/mol*K | PHPMS | Meot-Ner, 1984, 2 | gas phase; M |
By formula: Cl- + C2H4O2 = (Cl- • C2H4O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 24.40 ± 0.20 | kcal/mol | TDAs | Sieck, 1985 | gas phase; B,M |
ΔrH° | 21.6 ± 2.0 | kcal/mol | TDAs | Yamdagni and Kebarle, 1971 | gas phase; B,M |
ΔrH° | 23.9 ± 2.0 | kcal/mol | IMRE | Larson and McMahon, 1984 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 19.6 | cal/mol*K | PHPMS | Sieck, 1985 | gas phase; M |
ΔrS° | 24.0 | 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° | 19.3 | cal/mol*K | PHPMS | Yamdagni and Kebarle, 1971 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 18.60 ± 0.30 | kcal/mol | TDAs | Sieck, 1985 | gas phase; B |
ΔrG° | 15.8 ± 2.0 | kcal/mol | TDAs | Yamdagni and Kebarle, 1971 | gas phase; B |
ΔrG° | 16.7 ± 2.0 | kcal/mol | IMRE | Larson and McMahon, 1984 | gas phase; B,M |
By formula: F- + C2H4O2 = (F- • C2H4O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 44.1 ± 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 |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 25.6 | 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° | 36.5 ± 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- + C2H4O2 = (I- • C2H4O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 16.9 ± 1.0 | kcal/mol | TDAs | Caldwell and Kebarle, 1984 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 21.3 | cal/mol*K | PHPMS | Caldwell and Kebarle, 1984 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 10.5 ± 1.0 | kcal/mol | TDAs | Caldwell and Kebarle, 1984 | gas phase; B |
By formula: Li+ + C2H4O2 = (Li+ • C2H4O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 41.5 | kcal/mol | ICR | Staley and Beauchamp, 1975 | gas phase; switching reaction(Li+)H2O, from graph; Dzidic and Kebarle, 1970 interpolated; M |
+ = C2H4NO4-
By formula: NO2- + C2H4O2 = C2H4NO4-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrG° | 12.20 ± 0.20 | kcal/mol | IMRE | Viidanoja, Reiner, et al., 1998 | gas phase; B |
+ = C2H4NO5-
By formula: NO3- + C2H4O2 = C2H4NO5-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrG° | 11.80 ± 0.20 | kcal/mol | IMRE | Viidanoja, Reiner, et al., 1998 | gas phase; B |
References
Go To: Top, Gas phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics data, Ion clustering data, 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
Go To: Top, Gas phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics data, Ion clustering data, References
- Symbols used in this document:
AE Appearance energy Cp,gas Constant pressure heat capacity of gas IE (evaluated) Recommended ionization energy Pc Critical pressure S°gas Entropy of gas at standard conditions T Temperature Tboil Boiling point Tc Critical temperature Tfus Fusion (melting) point Ttriple Triple point temperature 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 ΔfusH Enthalpy of fusion ΔfusS Entropy of fusion ΔrG° Free energy of reaction at standard conditions ΔrH° Enthalpy of reaction at standard conditions ΔrS° Entropy of reaction at standard conditions 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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