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
- Permanent link for this species. Use this link for bookmarking this species for future reference.
- Information on this page:
- Other data available:
- Reaction thermochemistry data: reactions 51 to 79
- Gas phase ion energetics data
- Ion clustering data
- Gas Chromatography
- Data at other public NIST sites:
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Gas phase thermochemistry data
Go To: Top, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, IR Spectrum, Mass spectrum (electron ionization), UV/Visible spectrum, Vibrational and/or electronic energy levels, 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 | -433. ± 3. | kJ/mol | AVG | N/A | Average of 8 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
S°gas | 282.84 | J/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 (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
39.54 | 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 |
40.42 | 100. | ||
42.74 | 150. | ||
48.34 | 200. | ||
59.38 | 273.15 | ||
63.44 ± 0.11 | 298.15 | ||
63.74 | 300. | ||
79.66 | 400. | ||
93.93 | 500. | ||
106.18 | 600. | ||
116.63 | 700. | ||
125.50 | 800. | ||
132.99 | 900. | ||
139.26 | 1000. | ||
144.46 | 1100. | ||
148.76 | 1200. | ||
152.30 | 1300. | ||
155.22 | 1400. | ||
157.63 | 1500. |
Condensed phase thermochemistry data
Go To: Top, Gas phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, IR Spectrum, Mass spectrum (electron ionization), UV/Visible spectrum, Vibrational and/or electronic energy levels, 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 | -483.52 ± 0.36 | kJ/mol | Ccb | Steele, Chirico, et al., 1997 | ALS |
ΔfH°liquid | -484.5 ± 0.2 | kJ/mol | Ccb | Lebedeva, 1964 | ALS |
ΔfH°liquid | -484.1 ± 0.4 | kJ/mol | Ccb | Evans and Skinner, 1959 | ALS |
ΔfH°liquid | -487.0 | kJ/mol | Cm | Carson and Skinner, 1949 | Unpublished result by Rossini; ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -875.16 ± 0.34 | kJ/mol | Ccb | Steele, Chirico, et al., 1997 | Corresponding ΔfHºliquid = -483.52 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -874.2 ± 0.2 | kJ/mol | Ccb | Lebedeva, 1964 | Corresponding ΔfHºliquid = -484.47 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -874.5 ± 0.4 | kJ/mol | Ccb | Evans and Skinner, 1959 | Corresponding ΔfHºliquid = -484.1 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -872.4 | kJ/mol | Ccb | Schjanberg, 1935 | Corresponding ΔfHºliquid = -486.2 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
Quantity | Value | Units | Method | Reference | Comment |
S°liquid | 158.0 | J/mol*K | N/A | Martin and Andon, 1982 | DH |
S°liquid | 193.7 | J/mol*K | N/A | Parks and Kelley, 1925 | Extrapolation below 90 K. 76.82 J/mol*K.; DH |
Constant pressure heat capacity of liquid
Cp,liquid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
123.1 | 298.15 | Martin and Andon, 1982 | T = 13 to 450 K. Data also given by equation.; DH |
139.7 | 332. | Swietoslawski and Zielenkiewicz, 1958 | Mean value 22 to 96°C.; DH |
120.5 | 298. | Radulescu and Jula, 1934 | DH |
121.3 | 297.1 | Neumann, 1932 | T = 23.9 to 80.5°C. Value is unsmoothed experimental datum.; DH |
159.8 | 298.1 | Parks, Kelley, et al., 1929 | Extrapolation below 90 K, 42.68 J/mol*K. Revision of previous data.; DH |
123.4 | 294.7 | Parks and Kelley, 1925 | T = 87 to 295 K. Value is unsmoothed experimental datum.; DH |
137. | 287. to 335. | Pickering, 1895 | T = 260 to 335 K.; DH |
123.5 | 298. | von Reis, 1881 | T = 292 to 358 K.; DH |
Phase change data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Reaction thermochemistry data, Henry's Law data, IR Spectrum, Mass spectrum (electron ionization), UV/Visible spectrum, Vibrational and/or electronic energy levels, 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, 2 | Uncertainty assigned by TRC = 0.04 K; TRC |
Ttriple | 289.8 | K | N/A | Parks and Kelley, 1925, 2 | 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 | 57.81 | bar | N/A | Andereya and Chase, 1990 | Uncertainty assigned by TRC = 0.20 bar; TRC |
Pc | 58.2901 | bar | N/A | D'Souza and Teja, 1987 | Uncertainty assigned by TRC = 0.90 bar; Ambrose's procedure; TRC |
Pc | 57.86 | bar | N/A | Ambrose, Ellender, et al., 1977 | Uncertainty assigned by TRC = 0.08 bar; TRC |
Pc | 57.87 | bar | N/A | Young, 1910 | Uncertainty assigned by TRC = 1.0132 bar; TRC |
Pc | 57.867 | bar | N/A | Young, 1891 | Uncertainty assigned by TRC = 0.2666 bar; 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° | 50.3 | kJ/mol | CGC | Verevkin, 2000 | Based on data from 303. to 378. K.; AC |
ΔvapH° | 51.6 | kJ/mol | N/A | Majer and Svoboda, 1985 | |
ΔvapH° | 51.6 ± 1.5 | kJ/mol | C | Konicek and Wadso, 1970 | ALS |
ΔvapH° | 51.6 ± 1.6 | kJ/mol | C | Konicek, Wadsö, et al., 1970 | AC |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
23.7 | 391.1 | N/A | Majer and Svoboda, 1985 | |
39.1 | 360. | EB | Muñoz and Krähenbühl, 2001 | Based on data from 345. to 383. K.; AC |
40.9 | 335. | N/A | Vercher, Vázquez, et al., 2001 | Based on data from 320. to 395. K.; AC |
37.9 | 406. | A | Stephenson and Malanowski, 1987 | Based on data from 391. to 550. K.; AC |
42.0 | 305. | A | Stephenson and Malanowski, 1987 | Based on data from 290. to 396. K.; AC |
38.7 | 406. | A | Stephenson and Malanowski, 1987 | Based on data from 391. to 447. K.; AC |
38.1 | 452. | A | Stephenson and Malanowski, 1987 | Based on data from 437. to 535. K.; AC |
38.8 | 540. | A | Stephenson and Malanowski, 1987 | Based on data from 525. to 593. K.; AC |
41.6 | 304. | A | Stephenson and Malanowski, 1987 | Based on data from 289. to 392. K. See also Dykyj, 1970.; AC |
43.0 | 308. | N/A | Tamir, Dragoescu, et al., 1983 | AC |
40.3 | 340. | N/A | McDonald, Shrader, et al., 1959 | Based on data from 325. to 391. K.; AC |
41.6 | 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)
(kJ/mol)
Tr = reduced temperature (T / Tc)
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Temperature (K) | 298. to 392. |
---|---|
A (kJ/mol) | 22.84 |
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 (bar)
T = temperature (K)
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Temperature (K) | A | B | C | Reference |
---|---|---|---|---|
290.26 to 391.01 | 4.68206 | 1642.54 | -39.764 | McDonald, Shrader, et al., 1959 |
Enthalpy of sublimation
ΔsubH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
67. ± 1. | 223. | TE,ME | Calis-Van Ginkel, Calis, et al., 1978 | Based on data from 213. to 230. K.; AC |
70. ± 1. | 213. | TE,ME | Calis-Van Ginkel, Calis, et al., 1978 | Based on data from 213. to 230. K.; AC |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
11.72 | 298.7 | Domalski and Hearing, 1996 | See also Martin and Andon, 1982.; AC |
11.728 | 289.9 | Parks and Kelley, 1925 | DH |
10.83 | 289.8 | Louguinine and Dupont, 1911 | AC |
11.52 | 283.7 | Meyer, 1910 | AC |
11.126 | 290.06 | Pickering, 1895 | DH |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
40.47 | 289.9 | Parks and Kelley, 1925 | DH |
38.36 | 290.06 | Pickering, 1895 | DH |
Enthalpy of phase transition
ΔHtrs (kJ/mol) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
11.720 | 298.69 | crystaline, I | liquid | Martin and Andon, 1982 | DH |
Entropy of phase transition
ΔStrs (J/mol*K) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
40.5 | 298.69 | crystaline, I | liquid | Martin and Andon, 1982 | DH |
Reaction thermochemistry data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Henry's Law data, IR Spectrum, Mass spectrum (electron ionization), UV/Visible spectrum, Vibrational and/or electronic energy levels, 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
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
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.
Reactions 1 to 50
By formula: F- + C2H4O2 = (F- • C2H4O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 185. ± 8.4 | kJ/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° | 107. | J/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° | 153. ± 8.4 | kJ/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: C2H5O+ + C2H4O2 = (C2H5O+ • C2H4O2)
Bond type: Hydrogen bonds of the type OH-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 118. | kJ/mol | PHPMS | Meot-Ner (Mautner), 1992 | gas phase; M |
ΔrH° | 123. | kJ/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° | 118. | J/mol*K | PHPMS | Meot-Ner (Mautner), 1992 | gas phase; M |
ΔrS° | 117. | J/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° | 88.7 | kJ/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: Cl- + C2H4O2 = (Cl- • C2H4O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 102.1 ± 0.84 | kJ/mol | TDAs | Sieck, 1985 | gas phase; B,M |
ΔrH° | 90.4 ± 8.4 | kJ/mol | TDAs | Yamdagni and Kebarle, 1971 | gas phase; B,M |
ΔrH° | 100. ± 8.4 | kJ/mol | IMRE | Larson and McMahon, 1984 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 82.0 | J/mol*K | PHPMS | Sieck, 1985 | gas phase; M |
ΔrS° | 100. | J/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° | 80.8 | J/mol*K | PHPMS | Yamdagni and Kebarle, 1971 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 77.8 ± 1.3 | kJ/mol | TDAs | Sieck, 1985 | gas phase; B |
ΔrG° | 66.1 ± 8.4 | kJ/mol | TDAs | Yamdagni and Kebarle, 1971 | gas phase; B |
ΔrG° | 69.9 ± 8.4 | kJ/mol | IMRE | Larson and McMahon, 1984 | gas phase; B,M |
By formula: C2H3O2- + H+ = C2H4O2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1457. ± 5.9 | kJ/mol | CIDC | Angel and Ervin, 2006 | gas phase; B |
ΔrH° | 1456. ± 9.2 | kJ/mol | G+TS | Taft and Topsom, 1987 | gas phase; B |
ΔrH° | 1459. ± 8.8 | kJ/mol | G+TS | Cumming and Kebarle, 1978 | gas phase; B |
ΔrH° | 1459. ± 9.2 | kJ/mol | G+TS | Fujio, McIver, et al., 1981 | gas phase; value altered from reference due to change in acidity scale; B |
ΔrH° | 1435.9 ± 2.9 | kJ/mol | EIAE | Muftakhov, Vasil'ev, et al., 1999 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1427. ± 8.4 | kJ/mol | IMRE | Taft and Topsom, 1987 | gas phase; B |
ΔrG° | 1429. ± 8.4 | kJ/mol | IMRE | Cumming and Kebarle, 1978 | gas phase; B |
ΔrG° | 1430. ± 8.4 | kJ/mol | IMRE | Fujio, McIver, et al., 1981 | gas phase; value altered from reference due to change in acidity scale; B |
By formula: C2H7O+ + C2H4O2 = (C2H7O+ • C2H4O2)
Bond type: Hydrogen bonds of the type OH-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 123. | kJ/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° | 119. | J/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° | 87.0 | kJ/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+ + C2H4O2 = (CH6N+ • C2H4O2)
Bond type: Hydrogen bonds of the type NH+-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 92.0 | kJ/mol | PHPMS | Meot-Ner, 1984 | gas phase; M |
ΔrH° | 89.5 | kJ/mol | PHPMS | Meot-Ner, 1984 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 102. | J/mol*K | PHPMS | Meot-Ner, 1984 | gas phase; M |
ΔrS° | 100. | J/mol*K | N/A | Meot-Ner, 1984 | gas phase; Entropy change calculated or estimated; M |
Free energy of reaction
ΔrG° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
43.1 | 459. | PHPMS | Meot-Ner, 1984 | gas phase; Entropy change calculated or estimated; 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° | 50. | kJ/mol | PHPMS | Meot-Ner (Mautner), 1992 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 100. | J/mol*K | N/A | Meot-Ner (Mautner), 1992 | gas phase; Entropy change calculated or estimated; M |
Free energy of reaction
ΔrG° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
26. | 245. | PHPMS | Meot-Ner (Mautner), 1992 | gas phase; Entropy change calculated or estimated; M |
By formula: (C2H3O2- • 2C2H4O2 • H2O) + C2H4O2 = (C2H3O2- • 3C2H4O2 • H2O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 52.3 ± 2.5 | kJ/mol | N/A | Meot-ner, Elmore, et al., 1999 | gas phase; B |
ΔrH° | 67.8 ± 4.2 | kJ/mol | TDAs | Meot-Ner and Sieck, 1986 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 24.0 | kJ/mol | TDAs | Meot-ner, Elmore, et al., 1999 | gas phase; B |
ΔrG° | 26. ± 4.2 | kJ/mol | TDAs | Meot-Ner and Sieck, 1986 | gas phase; B |
By formula: (C2H3O2- • C2H4O2 • H2O) + C2H4O2 = (C2H3O2- • 2C2H4O2 • H2O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 82.4 ± 2.1 | kJ/mol | N/A | Meot-ner, Elmore, et al., 1999 | gas phase; B |
ΔrH° | 67.8 ± 4.2 | kJ/mol | TDAs | Meot-Ner and Sieck, 1986 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 45.23 | kJ/mol | TDAs | Meot-ner, Elmore, et al., 1999 | gas phase; B |
ΔrG° | 26. ± 4.2 | kJ/mol | TDAs | Meot-Ner and Sieck, 1986 | gas phase; B |
By formula: C2H3ClO + H2O = C2H4O2 + HCl
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -94.47 | kJ/mol | Cm | Devore and O'Neal, 1969 | liquid phase; Heat of hydrolysis; ALS |
ΔrH° | -92.30 | kJ/mol | Cm | Pritchard and Skinner, 1950 | liquid phase; Heat of hydrolysis at 298 K, see Carson and Skinner, 1949; ALS |
ΔrH° | -92.42 | kJ/mol | Cm | Carson and Skinner, 1949 | liquid phase; ALS |
By formula: C4H6O3 + H2O = 2C2H4O2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -56.6 ± 4.0 | kJ/mol | Cm | Becker and Maelicke, 1967 | liquid phase; ALS |
ΔrH° | -58.6 ± 0.4 | kJ/mol | Cm | Wadso, 1962 | liquid phase; ALS |
ΔrH° | -58.4 ± 0.4 | kJ/mol | Cm | Conn, Kistiakowsky, et al., 1942 | liquid phase; Heat of hydrolysis at 303 K; ALS |
By formula: I- + C2H4O2 = (I- • C2H4O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 70.7 ± 4.2 | kJ/mol | TDAs | Caldwell and Kebarle, 1984 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 89.1 | J/mol*K | PHPMS | Caldwell and Kebarle, 1984 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 43.9 ± 4.2 | kJ/mol | TDAs | Caldwell and Kebarle, 1984 | gas phase; B |
C2H3O2- + =
By formula: C2H3O2- + H+ = C2H4O2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1540. ± 13. | kJ/mol | G+TS | Grabowski and Cheng, 1989 | gas phase; B |
ΔrH° | 1539. ± 19. | kJ/mol | EIAE | Muftakhov, Vasil'ev, et al., 1999 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1511. ± 13. | kJ/mol | IMRB | Grabowski and Cheng, 1989 | gas phase; B |
By formula: C6H5NO2- + C2H4O2 = (C6H5NO2- • C2H4O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 94.56 ± 0.42 | kJ/mol | TDAs | Sieck, 1985 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 112. | J/mol*K | PHPMS | Sieck, 1985 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 61.09 ± 0.84 | kJ/mol | TDAs | Sieck, 1985 | gas phase; B |
By formula: C6H5O- + C2H4O2 = (C6H5O- • C2H4O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 115. | kJ/mol | PHPMS | Meot-Ner and Sieck, 1986 | gas phase; calculated from CH3COO-.C6H5OH; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 100. | J/mol*K | PHPMS | Meot-Ner and Sieck, 1986 | gas phase; calculated from CH3COO-.C6H5OH; 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° | 54.8 | kJ/mol | PHPMS | Meot-Ner (Mautner), 1992 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 93.7 | J/mol*K | PHPMS | Meot-Ner (Mautner), 1992 | gas phase; 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° | 77.4 | kJ/mol | PHPMS | Meot-Ner (Mautner), 1992 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 103. | J/mol*K | PHPMS | Meot-Ner (Mautner), 1992 | gas phase; M |
By formula: C6H12NO3+ + C2H4O2 = (C6H12NO3+ • C2H4O2)
Bond type: Hydrogen bonds with polydentate bonding in positive ions
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 75.7 | kJ/mol | PHPMS | Meot-Ner, 1984, 2 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 114. | J/mol*K | PHPMS | Meot-Ner, 1984, 2 | gas phase; M |
By formula: C4H7NO2 + H2O = C2H5NO + C2H4O2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -18.1 ± 0.2 | kJ/mol | Cm | Hill and Wadso, 1968 | solid phase; Heat of hydrolysis; ALS |
ΔrH° | -18.1 ± 0.2 | kJ/mol | Cm | Wadso, 1965 | solid phase; Heat of hydrolysis; ALS |
By formula: C4H10NO+ + C2H4O2 = (C4H10NO+ • C2H4O2)
Bond type: Hydrogen bonds of the type OH-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 77.0 | kJ/mol | PHPMS | Meot-Ner, 1984, 2 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 103. | J/mol*K | PHPMS | Meot-Ner, 1984, 2 | gas phase; M |
By formula: C2H3IO + H2O = HI + C2H4O2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -93.97 | kJ/mol | Cm | Devore and O'Neal, 1969 | liquid phase; Heat of hydrolysis; ALS |
ΔrH° | -90.33 | kJ/mol | Cm | Carson and Skinner, 1949 | liquid phase; Heat of hydrolysis; ALS |
By formula: (C2H3O2- • H2O) + C2H4O2 = (C2H3O2- • C2H4O2 • H2O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 123. ± 4.2 | kJ/mol | TDAs | Meot-Ner and Sieck, 1986 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 85.4 ± 6.7 | kJ/mol | TDAs | Meot-Ner and Sieck, 1986 | gas phase; B |
By formula: C4H6O3 + C4H11N = C6H13NO + C2H4O2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -113.2 ± 0.46 | kJ/mol | Cm | Wadso, 1962 | liquid phase; ALS |
ΔrH° | -163.7 ± 0.3 | kJ/mol | Cm | Wadso, 1958 | liquid phase; Heat of aminolysis; ALS |
By formula: C2H3BrO + H2O = HBr + C2H4O2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -97.53 | kJ/mol | Cm | Devore and O'Neal, 1969 | liquid phase; Heat of hydrolysis; ALS |
ΔrH° | -96.48 | kJ/mol | Cm | Carson and Skinner, 1949 | liquid phase; ALS |
+ = C8H9O2S-
By formula: C6H5S- + C2H4O2 = C8H9O2S-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 84.94 ± 0.42 | kJ/mol | TDAs | Sieck and Meot-ner, 1989 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 52.3 ± 1.7 | kJ/mol | TDAs | Sieck and Meot-ner, 1989 | gas phase; B |
By formula: (C2H3O2- • 2C2H4O2) + C2H4O2 = (C2H3O2- • 3C2H4O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 67.8 | kJ/mol | PHPMS | Meot-Ner and Sieck, 1986 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 139. | J/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° | 82.0 | kJ/mol | PHPMS | Meot-Ner and Sieck, 1986 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 120. | J/mol*K | PHPMS | Meot-Ner and Sieck, 1986 | gas phase; M |
By formula: C6H5S- + C2H4O2 = (C6H5S- • C2H4O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 84.9 | kJ/mol | PHPMS | Sieck and Meot-ner, 1989 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 110. | J/mol*K | PHPMS | Sieck and Meot-ner, 1989 | gas phase; M |
By formula: Li+ + C2H4O2 = (Li+ • C2H4O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 174. | kJ/mol | ICR | Staley and Beauchamp, 1975 | gas phase; switching reaction(Li+)H2O, from graph; Dzidic and Kebarle, 1970 interpolated; M |
By formula: C2H3O2- + C2H4O2 = (C2H3O2- • C2H4O2)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 123. | kJ/mol | PHPMS | Meot-Ner and Sieck, 1986 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 124. | J/mol*K | PHPMS | Meot-Ner and Sieck, 1986 | gas phase; M |
By formula: C8H14O4 + 2H2O = C4H10O2 + 2C2H4O2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -22.3 ± 2.1 | kJ/mol | Cm | Shlechter, Othmer, et al., 1945 | liquid phase; Heat of formation derived by Cox and Pilcher, 1970; ALS |
By formula: C5H6N2O + H2O = C3H4N2 + C2H4O2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -20.2 ± 0.2 | kJ/mol | Cm | Wadso, 1960 | liquid phase; solvent: Aqueous; Heat of hydrolysis; ALS |
By formula: C4H10O2 + 2C2H4O2 = C8H14O4 + 2H2O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 22.30 | kJ/mol | Eqk | Shlechter, Othmer, et al., 1945 | liquid phase; Heat of esterification at 338-453 K; ALS |
By formula: C6H12O3 + C2H4O2 = C8H14O4 + H2O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1.85 | kJ/mol | Eqk | Shlechter, Othmer, et al., 1945 | liquid phase; Heat of esterification at 338-453 K; ALS |
By formula: C6H9NO3 + 2H2O = C2H5NO + 2C2H4O2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -103.5 ± 0.08 | kJ/mol | Cm | Hill and Wadso, 1968 | liquid phase; Heat of hydrolysis; ALS |
By formula: 2H2O + C4H8O2 = C2H4O2 + 2CH4O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -74.4 ± 3.6 | kJ/mol | Cm | Guthrie and Liu, 1995 | liquid phase; Heat of hydrolysis; ALS |
By formula: C10H14 + C2H4O2 = C12H18O2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -182.0 ± 0.3 | kJ/mol | Cac | Wiberg, Connon, et al., 1979 | liquid phase; solvent: Acetic acid; ALS |
By formula: C2H4OS + H2O = C2H4O2 + H2S
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -2.7 ± 0.3 | kJ/mol | Cm | Sunner and Wadso, 1957 | liquid phase; Heat of hydrolysis; ALS |
By formula: C2H5NO + H2O = C2H4O2 + H3N
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 76.1 ± 1.4 | kJ/mol | Cm | Hill and Wadso, 1968 | solid phase; Heat of hydrolysis; ALS |
By formula: C6H13NO + C2H4O2 = C8H15NO2 + H2O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 40.5 ± 0.50 | kJ/mol | Cm | Wadso, 1965 | liquid phase; Heat of hydrolysis; ALS |
By formula: C5H10OS + H2O = C3H8S + C2H4O2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -3.9 ± 0.3 | kJ/mol | Cm | Wadso, 1957 | liquid phase; Heat of hydrolysis; ALS |
+ = C10H11NO2 +
By formula: C8H9NO + C2H4O2 = C10H11NO2 + H2O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 45.5 ± 0.3 | kJ/mol | Cm | Wadso, 1965 | solid phase; Heat of hydrolysis; ALS |
By formula: C9H10O2 + H2O = C7H8O + C2H4O2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -18.4 ± 0.59 | kJ/mol | Cm | Sunner, 1957 | liquid phase; Heat of hydrolysis; ALS |
By formula: H2O + C6H12OS = C4H10S + C2H4O2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -4.6 ± 0.3 | kJ/mol | Cm | Wadso, 1957 | liquid phase; Heat of hydrolysis; ALS |
By formula: C3H4N4O + H2O = CH2N4 + C2H4O2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -43.1 ± 0.4 | kJ/mol | Cm | Wadso, 1960 | solid phase; Heat of hydrolysis; ALS |
By formula: C9H8O3S + H2O = C7H6O2S + C2H4O2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -11.5 ± 0.4 | kJ/mol | Cm | Nelander, 1964 | solid phase; Heat of hydrolysis; ALS |
By formula: C8H9NO + H2O = C6H7N + C2H4O2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -42.0 ± 0.3 | kJ/mol | Cm | Wadso, 1965 | solid phase; Heat of hydrolysis; ALS |
By formula: C2H4O2 + C3H6O = C5H8O2 + H2O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 60.2 ± 0.3 | kJ/mol | Cm | Sunner, 1957 | liquid phase; Heat of hydrolysis; ALS |
By formula: C4H8OS + H2O = C2H4O2 + C2H6S
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -4.0 ± 0.3 | kJ/mol | Cm | Wadso, 1957 | liquid phase; Heat of hydrolysis; ALS |
By formula: H2O + C5H10OS = C2H4O2 + C3H8S
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -5.8 ± 0.3 | kJ/mol | Cm | Wadso, 1957 | liquid phase; Heat of hydrolysis; ALS |
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 | 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 |
IR Spectrum
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Data compiled by: Coblentz Society, Inc.
- GAS (15 mmHg, N2 ADDED, TOTAL PRESSURE 600 mmHg); DOW KBr FOREPRISM-GRATING; DIGITIZED BY COBLENTZ SOCIETY (BATCH I) FROM HARD COPY; 2 cm-1 resolution
- SOLUTION (10% IN CCl4 FOR 3800-1300, 10% IN CS2 FOR 1300-650, 10% IN CCl4 FOR 650-250 CM-1) VERSUS SOLVENT; PERKIN-ELMER 521 (GRATING); DIGITIZED BY NIST FROM HARD COPY (FROM TWO SEGMENTS); 4 cm-1 resolution
Data compiled by: NIST Mass Spectrometry Data Center, William E. Wallace, director
Mass spectrum (electron ionization)
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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: NIST Mass Spectrometry Data Center, William E. Wallace, director
Spectrum
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Additional Data
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Due to licensing restrictions, this spectrum cannot be downloaded.
Owner | NIST Mass Spectrometry Data Center Collection (C) 2014 copyright by the U.S. Secretary of Commerce on behalf of the United States of America. All rights reserved. |
---|---|
Origin | Japan AIST/NIMC Database- Spectrum MS-NW- 80 |
NIST MS number | 227635 |
UV/Visible spectrum
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, IR Spectrum, Mass spectrum (electron ionization), Vibrational and/or electronic energy levels, 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: Victor Talrose, Eugeny B. Stern, Antonina A. Goncharova, Natalia A. Messineva, Natalia V. Trusova, Margarita V. Efimkina
Spectrum
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Additional Data
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Download spectrum in JCAMP-DX format.
Source | Briegleb and Strohmeier, 1946 |
---|---|
Owner | INEP CP RAS, NIST OSRD Collection (C) 2007 copyright by the U.S. Secretary of Commerce on behalf of the United States of America. All rights reserved. |
Origin | INSTITUTE OF ENERGY PROBLEMS OF CHEMICAL PHYSICS, RAS |
Source reference | RAS UV No. 2843 |
Instrument | n.i.g. |
Sample temp. (C) | 210 |
Sample pressure | 309 mm Hg |
Melting point | 16.6 |
Boiling point | 117.9 |
Vibrational and/or electronic energy levels
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, IR Spectrum, Mass spectrum (electron ionization), UV/Visible spectrum, 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: Takehiko Shimanouchi
Symmetry: Cs Symmetry Number σ = 1
Sym. | No | Approximate | Selected Freq. | Infrared | Raman | Comments | ||||
---|---|---|---|---|---|---|---|---|---|---|
Species | type of mode | Value | Rating | Value | Phase | Value | Phase | |||
a' | 1 | OH str | 3583 | B | 3583 M | gas | ||||
a' | 2 | CH3 d-str | 3051 | B | 3051 VW | gas | ||||
a' | 3 | CH3 s-str | 2944 | B | 2944 VW | gas | ||||
a' | 4 | C=O str | 1788 | B | 1788 VS | gas | ||||
a' | 5 | CH3 d-deform | 1430 | C | 1430 sh | gas | SF(ν14) | |||
a' | 6 | CH3 s-deform | 1382 | B | 1382 M | gas | ||||
a' | 7 | OH bend | 1264 | B | 1264 M | gas | ||||
a' | 8 | C-O str | 1182 | B | 1182 S | gas | ||||
a' | 9 | CH3 rock | 989 | B | 989 M | gas | ||||
a' | 10 | CC str | 847 | B | 847 W | gas | ||||
a' | 11 | OCO deform | 657 | B | 657 S | gas | ||||
a' | 12 | CCO deform | 581 | B | 581 M | gas | ||||
a | 13 | CH3 d-str | 2996 | B | 2996 VW | gas | ||||
a | 14 | CH3 d-deform | 1430 | C | 1430 sh | gas | SF(ν5) | |||
a | 15 | CH3 rock | 1048 | B | 1048 W | gas | ||||
a | 16 | C=O op-bend | 642 | B | 642 S | gas | ||||
a | 17 | C-O torsion | 534 | B | 534 M | gas | ||||
a | 18 | CH3 torsion | 93 | E | CF | |||||
Source: Shimanouchi, 1972
Notes
VS | Very strong |
S | Strong |
M | Medium |
W | Weak |
VW | Very weak |
sh | Shoulder |
CF | Calculated frequency |
SF | Calculation shows that the frequency approximately equals that of the vibration indicated in the parentheses. |
B | 1~3 cm-1 uncertainty |
C | 3~6 cm-1 uncertainty |
E | 15~30 cm-1 uncertainty |
References
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, IR Spectrum, Mass spectrum (electron ionization), UV/Visible spectrum, Vibrational and/or electronic energy levels, 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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Die specifische Wärme flüssiger organischer Verbindungen und ihre Beziehung zu deren Moleculargewicht,
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Thermodynamic properties of organic oxygen compounds. Part LII. Molar heat capacity of ethanoic, propanoic, and butanoic acids.,
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Thermal Data on Organic Compounds II. The Heat Capacities of Five Organic Compounds. The Entropies and Free Energies of Some Homologous Series of Aliphatic Compounds,
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The Internal Heat of Vaporization constants of thirty pure substances,
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Notes
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- Symbols used in this document:
Cp,gas Constant pressure heat capacity of gas Cp,liquid Constant pressure heat capacity of liquid Pc Critical pressure S°gas Entropy of gas at standard conditions S°liquid Entropy of liquid 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 ΔcH°liquid Enthalpy of combustion of liquid at standard conditions ΔfH°gas Enthalpy of formation of gas 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 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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