Acetaldehyde
- Formula: C2H4O
- Molecular weight: 44.0526
- IUPAC Standard InChIKey: IKHGUXGNUITLKF-UHFFFAOYSA-N
- CAS Registry Number: 75-07-0
- 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: Acetic aldehyde; Ethanal; Ethyl aldehyde; CH3CHO; Acetaldehyd; Aldehyde acetique; Aldeide acetica; NCI-C56326; Octowy aldehyd; Acetylaldehyde; Rcra waste number U001; UN 1089; NSC 7594
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Gas phase thermochemistry data
Go To: Top, Condensed phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics data, Ion clustering data, Mass spectrum (electron ionization), 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
GT - Glushko Thermocenter, Russian Academy of Sciences, Moscow
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°gas | -170.7 ± 1.5 | kJ/mol | Chyd | Wiberg, Crocker, et al., 1991 | ALS |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
35.53 | 50. | Thermodynamics Research Center, 1997 | 1 bar. Recommended heat capacity and entropy values are in good agreement with statistically calculated values of [ Pitzer K.S., 1949, 66LIP/WAG]. Discrepancies with results of calculation [ Della Vedova C.O., 1991] amount to 1.4 J/mol*K for S(300 K) and 3.4 J/mol*K for Cp(900 K). S(298.15 K) value calculated by high accuracy ab initio method [ East A.L.L., 1997] is in close agreement with selected one. Please also see Chao J., 1980, Chao J., 1986.; GT |
40.27 | 100. | ||
43.26 | 150. | ||
46.47 | 200. | ||
52.80 | 273.15 | ||
55.32 ± 0.08 | 298.15 | ||
55.51 | 300. | ||
66.28 | 400. | ||
76.68 | 500. | ||
85.94 | 600. | ||
94.04 | 700. | ||
101.07 | 800. | ||
107.19 | 900. | ||
112.49 | 1000. | ||
117.08 | 1100. | ||
121.06 | 1200. | ||
124.50 | 1300. | ||
127.49 | 1400. | ||
130.09 | 1500. | ||
135.22 | 1750. | ||
138.94 | 2000. | ||
141.68 | 2250. | ||
143.75 | 2500. | ||
145.35 | 2750. | ||
146.59 | 3000. |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
54.98 | 298.1 | Chao J., 1986 | These ideal gas heat capacity values were obtained from the observed values of [ Coleman C.F., 1949] using the second virial coefficient data from [ Pitzer K.S., 1949].; GT |
58.03 | 322.9 | ||
62.43 | 372.7 | ||
67.45 | 422.4 |
Condensed phase thermochemistry data
Go To: Top, Gas phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics data, Ion clustering data, Mass spectrum (electron ionization), 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 | -196.4 ± 1.5 | kJ/mol | Chyd | Wiberg, Crocker, et al., 1991 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
S°liquid | 117.3 | J/mol*K | N/A | Lebedev and Vasil'ev, 1988 | DH |
Constant pressure heat capacity of liquid
Cp,liquid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
89.05 | 298.15 | Lebedev and Vasil'ev, 1988 | T = 15 to 300 K.; DH |
96.21 | 273. | Connor, Elving, et al., 1947 | DH |
Phase change 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 as indicated in comments:
BS - Robert L. Brown and Stephen E. Stein
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, Chris Muzny director
DRB - Donald R. Burgess, Jr.
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
CAL - James S. Chickos, William E. Acree, Jr., Joel F. Liebman, Students of Chem 202 (Introduction to the Literature of Chemistry), University of Missouri -- St. Louis
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 294.0 ± 0.8 | K | AVG | N/A | Average of 25 out of 27 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 151. ± 3. | K | AVG | N/A | Average of 15 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 466.0 | K | N/A | Teja and Anselme, 1990 | Uncertainty assigned by TRC = 2. K; TRC |
Tc | 461. | K | N/A | Hollmann, 1903 | Uncertainty assigned by TRC = 2. K; TRC |
Tc | 454.7 | K | N/A | Van der Waals, 1881 | Uncertainty assigned by TRC = 6. K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 6.49 | mol/l | N/A | Teja and Anselme, 1990 | Uncertainty assigned by TRC = 0.1 mol/l; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 26.12 | kJ/mol | N/A | Majer and Svoboda, 1985 | |
ΔvapH° | 25.7 | kJ/mol | N/A | Wiberg, Crocker, et al., 1991 | DRB |
ΔvapH° | 26.9 | kJ/mol | EB | Bull, Seregrennaja, et al., 1963 | Based on data from 293. to 377. K. See also Verevkin, Krasnykh, et al., 2003.; AC |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
25.76 | 293.3 | N/A | Majer and Svoboda, 1985 | |
26.0 | 308. | A | Stephenson and Malanowski, 1987 | Based on data from 293. to 377. K.; AC |
27.6 | 283. | A | Stephenson and Malanowski, 1987 | Based on data from 272. to 294. K. See also Dykyj, 1970.; AC |
26.3 | 308. | N/A | Kim and Kim, 1977 | Based on data from 293. to 345. K.; AC |
27.0 | 307. | N/A | Coles and Popper, 1950 | Based on data from 273. to 307. K.; AC |
25.7 ± 0.2 | 294. | V | Coleman and DeVries, 1949 | ALS |
Antoine Equation Parameters
log10(P) = A − (B / (T + C))
P = vapor pressure (bar)
T = temperature (K)
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Temperature (K) | A | B | C | Reference | Comment |
---|---|---|---|---|---|
293.4 to 377.5 | 3.68639 | 822.894 | -69.899 | Bull, Seregrennaja, et al., 1963, 2 | Coefficents calculated by NIST from author's data. |
272.9 to 307.6 | 5.1883 | 1637.083 | 22.317 | Coles and Popper, 1950 | Coefficents calculated by NIST from author's data. |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
2.310 | 149.78 | Lebedev and Vasil'ev, 1988 | DH |
1.72 | 242.9 | Domalski and Hearing, 1996 | AC |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
15.43 | 149.78 | Lebedev and Vasil'ev, 1988 | DH |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
15.42 | 149.8 | Domalski and Hearing, 1996 | CAL |
7.06 | 242.9 |
Enthalpy of phase transition
ΔHtrs (kJ/mol) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
1.716 | 242.9 | liquid | liquid | Lebedev and Vasil'ev, 1988 | Lambda type transition.; DH |
Entropy of phase transition
ΔStrs (J/mol*K) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
7.35 | 242.9 | liquid | liquid | Lebedev and Vasil'ev, 1988 | Lambda; DH |
Henry's Law data
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Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data compiled by: Rolf Sander
Henry's Law constant (water solution)
kH(T) = k°H exp(d(ln(kH))/d(1/T) ((1/T) - 1/(298.15 K)))
k°H = Henry's law constant for solubility in water at 298.15 K (mol/(kg*bar))
d(ln(kH))/d(1/T) = Temperature dependence constant (K)
k°H (mol/(kg*bar)) | d(ln(kH))/d(1/T) (K) | Method | Reference | Comment |
---|---|---|---|---|
14. | 5600. | L | N/A | |
13. | 5700. | M | N/A | |
9.8 | Q | N/A | missing citation give several references for the Henry's law constants but don't assign them to specific species. | |
17. | 5000. | M | N/A | The data from Table 1 by missing citation was used to redo the regression analysis. The data for acetone in their Table 2 is wrong. |
11. | 6300. | M | N/A | missing citation list effective values that take into account hydration of the aldehydes: kH = ([RCHO] + [RCH(OH)2]) / p(RCHO) |
1.7 | 4500. | X | N/A | |
13. | 5800. | M | N/A | |
15. | X | N/A | Value given here as quoted by missing citation. | |
17. | 4700. | X | N/A | |
15. | M | Buttery, Ling, et al., 1969 | ||
15. | X | N/A | Value given here as quoted by missing citation. |
Gas phase ion energetics data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Henry's Law data, Ion clustering data, Mass spectrum (electron ionization), References, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data evaluated as indicated in comments:
HL - Edward P. Hunter and Sharon G. Lias
L - Sharon G. Lias
Data compiled as indicated in comments:
B - John E. Bartmess
LBLHLM - Sharon G. Lias, John E. Bartmess, Joel F. Liebman, John L. Holmes, Rhoda D. Levin, and W. Gary Mallard
LLK - Sharon G. Lias, Rhoda D. Levin, and Sherif A. Kafafi
RDSH - Henry M. Rosenstock, Keith Draxl, Bruce W. Steiner, and John T. Herron
View reactions leading to C2H4O+ (ion structure unspecified)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
IE (evaluated) | 10.229 ± 0.0007 | eV | N/A | N/A | L |
Quantity | Value | Units | Method | Reference | Comment |
Proton affinity (review) | 768.5 | kJ/mol | N/A | Hunter and Lias, 1998 | HL |
Quantity | Value | Units | Method | Reference | Comment |
Gas basicity | 736.5 | kJ/mol | N/A | Hunter and Lias, 1998 | HL |
Electron affinity determinations
EA (eV) | Method | Reference | Comment |
---|---|---|---|
0.00035 | EFD | Desfrancois, Abdoul-Carime, et al., 1994 | EA: 0.36 meV. Dipole-bound state.; B |
Ionization energy determinations
Appearance energy determinations
De-protonation reactions
C2H3O- + =
By formula: C2H3O- + H+ = C2H4O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1533.1 ± 3.4 | kJ/mol | D-EA | Mead, Lykke, et al., 1984 | gas phase; Uncertainty: 6 millical/mol (0.26 micro-eV).Dipolebound state at ca. 14.3 cal/mol (5 cm-1); B |
ΔrH° | 1531. ± 9.2 | kJ/mol | G+TS | Bartmess, Scott, et al., 1979 | gas phase; Acid: ethanal. The enol is 9.6 kcal/mol more acidic: Holmes and Lossing, 1982; value altered from reference due to change in acidity scale; B |
ΔrH° | 1533. ± 12. | kJ/mol | G+TS | Cumming and Kebarle, 1978 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1505. ± 5.0 | kJ/mol | H-TS | Mead, Lykke, et al., 1984 | gas phase; Uncertainty: 6 millical/mol (0.26 micro-eV).Dipolebound state at ca. 14.3 cal/mol (5 cm-1); B |
ΔrG° | 1502. ± 8.4 | kJ/mol | IMRE | Bartmess, Scott, et al., 1979 | gas phase; Acid: ethanal. The enol is 9.6 kcal/mol more acidic: Holmes and Lossing, 1982; value altered from reference due to change in acidity scale; B |
ΔrG° | 1505. ± 8.4 | kJ/mol | IMRE | Cumming and Kebarle, 1978 | gas phase; B |
C2H3O- + =
By formula: C2H3O- + H+ = C2H4O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1645.1 ± 4.0 | kJ/mol | D-EA | Nimlos, Soderquist, et al., 1989 | gas phase; B |
ΔrH° | 1636. ± 8.8 | kJ/mol | G+TS | DePuy, Bierbaum, et al., 1985 | gas phase; B |
ΔrH° | 1619. ± 33. | kJ/mol | CIDT | Graul and Squires, 1990 | gas phase; B |
ΔrH° | <1598.3 | kJ/mol | CIDT | Graul and Squires, 1988 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1613. ± 4.6 | kJ/mol | H-TS | Nimlos, Soderquist, et al., 1989 | gas phase; B |
ΔrG° | 1604. ± 8.4 | kJ/mol | IMRB | DePuy, Bierbaum, et al., 1985 | gas phase; B |
ΔrG° | <1565.9 ± 2.5 | kJ/mol | H-TS | Graul and Squires, 1988 | gas phase; B |
Ion clustering data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics data, Mass spectrum (electron ionization), 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:
RCD - Robert C. Dunbar
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
By formula: Ag+ + C2H4O = (Ag+ • C2H4O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 182. ± 19. | kJ/mol | RAK | Ho, Yang, et al., 1997 | RCD |
By formula: C2H3O2- + C2H4O = (C2H3O2- • C2H4O)
Bond type: Hydrogen bonds of deprotonated acids to ketones/
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 68.2 ± 4.2 | kJ/mol | TDAs | Meot-ner, 1988 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 90.8 | J/mol*K | PHPMS | Meot-ner, 1988 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 41. ± 8.4 | kJ/mol | TDAs | Meot-ner, 1988 | gas phase; B |
By formula: C2H5O+ + C2H4O = (C2H5O+ • C2H4O)
Bond type: Hydrogen bonds of the type OH-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 133. | 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; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 121. | 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; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 97.5 | 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; M |
By formula: C2H5O+ + C2H4O = (C2H5O+ • C2H4O)
Bond type: Hydrogen bonds of the type OH-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 121. | 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° | 110. | 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 |
(C2H5O- • 4294967295) + = C2H5O-
By formula: (C2H5O- • 4294967295C2H4O) + C2H4O = C2H5O-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 158. ± 4.2 | kJ/mol | N/A | Ramond, Davico, et al., 2000 | gas phase; B |
ΔrH° | 165. ± 9.2 | kJ/mol | Ther | Bartmess, Scott, et al., 1979 | gas phase; value altered from reference due to change in acidity scale; B |
By formula: C2H7O+ + C2H4O = (C2H7O+ • C2H4O)
Bond type: Hydrogen bonds of the type OH-O between organics
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 131. | 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° | 113. | 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° | 97.1 | 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- + C2H4O = (Cl- • C2H4O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 60.2 ± 8.4 | kJ/mol | IMRE | Larson and McMahon, 1984 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 90.8 | J/mol*K | N/A | Larson and McMahon, 1984 | gas phase; switching reaction(Cl-)t-C4H9F, Entropy change calculated or estimated; Larson and McMahon, 1984, 2; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 33. ± 8.4 | kJ/mol | IMRE | Larson and McMahon, 1984 | gas phase; B,M |
By formula: Li+ + C2H4O = (Li+ • C2H4O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 173. | kJ/mol | ICR | Staley and Beauchamp, 1975 | gas phase; switching reaction(Li+)H2O, Keesee and Castleman, 1986 from Berman and Beauchamp, 1986; Dzidic and Kebarle, 1970 interpolated; M |
By formula: Mg+ + C2H4O = (Mg+ • C2H4O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 260. ± 20. | kJ/mol | ICR | Operti, Tews, et al., 1988 | gas phase; switching reaction,Thermochemical ladder(Mg+)CH3OH; M |
By formula: NO- + C2H4O = (NO- • C2H4O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 164. | kJ/mol | ICR | Reents and Freiser, 1981 | gas phase; switching reaction,Thermochemical ladder(NO+)C2H5OH, Entropy change calculated or estimated; Farid and McMahon, 1978; M |
By formula: Na+ + C2H4O = (Na+ • C2H4O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 113. ± 3. | kJ/mol | CIDT | Armentrout and Rodgers, 2000 | RCD |
Mass spectrum (electron ionization)
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, 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 by: NIST Mass Spectrometry Data Center, William E. Wallace, director
Spectrum
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Additional Data
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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-9104 |
NIST MS number | 227634 |
References
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics data, Ion clustering data, Mass spectrum (electron ionization), Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Wiberg, Crocker, et al., 1991
Wiberg, K.B.; Crocker, L.S.; Morgan, K.M.,
Thermochemical studies of carbonyl compounds. 5. Enthalpies of reduction of carbonyl groups,
J. Am. Chem. Soc., 1991, 113, 3447-3450. [all data]
Thermodynamics Research Center, 1997
Thermodynamics Research Center,
Selected Values of Properties of Chemical Compounds., Thermodynamics Research Center, Texas A&M University, College Station, Texas, 1997. [all data]
Pitzer K.S., 1949
Pitzer K.S., Jr.,
Thermodynamics and vibrational spectrum of acetaldehyde,
J. Am. Chem. Soc., 1949, 71, 2842-2844. [all data]
Della Vedova C.O., 1991
Della Vedova C.O.,
Raman and infrared spectra and photochemical behavior of acetaldehyde isolated in matrixes,
J. Raman Spectrosc., 1991, 22, 505-507. [all data]
East A.L.L., 1997
East A.L.L.,
Ab initio statistical thermodynamical models for the computation of third-law entropies,
J. Chem. Phys., 1997, 106, 6655-6674. [all data]
Chao J., 1980
Chao J.,
Perfect gas thermodynamic properties of methanal, ethanal and their deuterated species,
Thermochim. Acta, 1980, 41, 41-54. [all data]
Chao J., 1986
Chao J.,
Thermodynamic properties of key organic oxygen compounds in the carbon range C1 to C4. Part 2. Ideal gas properties,
J. Phys. Chem. Ref. Data, 1986, 15, 1369-1436. [all data]
Coleman C.F., 1949
Coleman C.F.,
The heat capacity of organic vapors. V. Acetaldehyde,
J. Am. Chem. Soc., 1949, 71, 2839-2841. [all data]
Lebedev and Vasil'ev, 1988
Lebedev, B.V.; Vasil'ev, V.G.,
Thermodynamics of ethanal at 0-300 K,
Zhur. Fiz. Khim., 1988, 62, 3099-3102. [all data]
Connor, Elving, et al., 1947
Connor, A.Z.; Elving, P.J.; Steingiser, S.,
Specific heat of acetaldehyde and acetaldehyde dibutyl acetal,
J. Am. Chem. Soc., 1947, 69, 1532. [all data]
Teja and Anselme, 1990
Teja, A.S.; Anselme, M.J.,
The critical properties of thermally stable and unstable fluids. I. 1985 results,
AIChE Symp. Ser., 1990, 86, 279, 115-21. [all data]
Hollmann, 1903
Hollmann, R.,
Physical and natural equilibria between the modifications of aldehyde,
Z. Phys. Chem., Stoechiom. Verwandtschaftsl., 1903, 43, 129-59. [all data]
Van der Waals, 1881
Van der Waals, J.D.,
Continuity of Gas and Liquid Data, 1881,, 1881, Leipzig, p 168. [all data]
Majer and Svoboda, 1985
Majer, V.; Svoboda, V.,
Enthalpies of Vaporization of Organic Compounds: A Critical Review and Data Compilation, Blackwell Scientific Publications, Oxford, 1985, 300. [all data]
Bull, Seregrennaja, et al., 1963
Bull, S.S.; Seregrennaja, I.I.; Tsherbakora, P.R.,
Khim. Prom. (Moscow), 1963, 7, 507. [all data]
Verevkin, Krasnykh, et al., 2003
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Fragment ions from CH3CHO and (CH3)2CO by electron impact,
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Notes
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics data, Ion clustering data, Mass spectrum (electron ionization), References
- Symbols used in this document:
AE Appearance energy Cp,gas Constant pressure heat capacity of gas Cp,liquid Constant pressure heat capacity of liquid EA Electron affinity IE (evaluated) Recommended ionization energy S°liquid Entropy of liquid at standard conditions Tboil Boiling point Tc Critical temperature Tfus Fusion (melting) point d(ln(kH))/d(1/T) Temperature dependence parameter for Henry's Law constant k°H Henry's Law constant at 298.15K ΔHtrs Enthalpy of phase transition ΔStrs Entropy of phase transition 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 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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