Ethyl Acetate

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Gas phase thermochemistry data

Go To: Top, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Gas phase ion energetics data, Ion clustering data, References, Notes

Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.

Data compiled as indicated in comments:
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
DRB - Donald R. Burgess, Jr.
GT - Glushko Thermocenter, Russian Academy of Sciences, Moscow

Quantity Value Units Method Reference Comment
Δfgas-106.46 ± 0.20kcal/molCmWiberg, Crocker, et al., 1991ALS
Δfgas-106.3 ± 0.1kcal/molCmWiberg and Waldron, 1991Heat of hydrolysis; ALS
Δfgas-106.1kcal/molN/AFenwick, Harrop, et al., 1978Value computed using ΔfHliquid° value of -478.8±0.7 kj/mol from Fenwick, Harrop, et al., 1978 and ΔvapH° value of 35.1 kj/mol from Wiberg and Waldron, 1991.; DRB
Δfgas-106.8kcal/molN/AButwill and Rockenfeller, 1970Value computed using ΔfHliquid° value of -482.0±4.0 kj/mol from Butwill and Rockenfeller, 1970 and ΔvapH° value of 35.1 kj/mol from Wiberg and Waldron, 1991.; DRB
Quantity Value Units Method Reference Comment
gas86.699cal/mol*KN/AStull D.R., 1969The value of 377.02 J/mol*K was determined from equilibrium study [ Vvedenskii A.A., 1949]. The S(298.15 K)=365.6 J/mol*K was calculated from data for related compounds by difference method [ Dorofeeva O.V., 1997]. Please also see Parks G.S., 1933.; GT

Constant pressure heat capacity of gas

Cp,gas (cal/mol*K) Temperature (K) Reference Comment
30.072360.Connett J.E., 1976GT
31.324380.
32.557400.
34.130425.
35.724450.

Constant pressure heat capacity of gas

Cp,gas (cal/mol*K) Temperature (K) Reference Comment
27.161298.15Stull D.R., 1969Selected values were based on extrapolation of heat capacity data [ Bennewitz K., 1938, Jatkar S.K.K., 1939] to high temperatures.; GT
27.239300.
32.839400.
38.700500.
43.650600.
47.689700.
51.011800.
53.750900.
56.0491000.

Condensed phase thermochemistry data

Go To: Top, Gas phase thermochemistry data, Phase change data, Reaction thermochemistry data, Gas phase ion energetics data, Ion clustering data, References, Notes

Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.

Data compiled 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
Δfliquid-114.86 ± 0.19kcal/molCmWiberg, Crocker, et al., 1991ALS
Δfliquid-114.69 ± 0.11kcal/molCmWiberg and Waldron, 1991Heat of hydrolysis; ALS
Δfliquid-114.44 ± 0.17kcal/molCcbFenwick, Harrop, et al., 1978ALS
Δfliquid-115.20 ± 0.95kcal/molCcbButwill and Rockenfeller, 1970ALS
Quantity Value Units Method Reference Comment
Δcliquid-535.02 ± 0.11kcal/molCcbFenwick, Harrop, et al., 1978Corresponding Δfliquid = -114.44 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS
Δcliquid-534.27 ± 0.94kcal/molCcbButwill and Rockenfeller, 1970Corresponding Δfliquid = -115.19 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS
Δcliquid-539.1kcal/molCcbRoth and Muller, 1929Corresponding Δfliquid = -110.4 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS
Δcliquid-536.9kcal/molCcbGuinchant, 1918Corresponding Δfliquid = -112.6 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS
Quantity Value Units Method Reference Comment
liquid62.00cal/mol*KN/AParks, Huffman, et al., 1933Extrapolation below 90 K, 62.80 J/mol*K.; DH

Constant pressure heat capacity of liquid

Cp,liquid (cal/mol*K) Temperature (K) Reference Comment
40.378298.15Pintos, Bravo, et al., 1988DH
40.772298.32Zabransky, Hynek, et al., 1987T = 294 to 340 K. Unsmoothed experimental datum.; DH
40.464298.15Jimenez, Romani, et al., 1986DH
40.406298.15Baluja, Bravo, et al., 1985DH
40.54298.15Costas and Patterson, 1985T = 283.15, 298.15, 313.15 K.; DH
40.54298.15Costas and Patterson, 1985, 2DH
40.01298.15Fuchs, 1979DH
40.51298.1Roux, Perron, et al., 1978T = 283 to 313 K.; DH
40.349303.61Zhdanov, 1945T = 5 to 46°C. Value is unsmoothed experimental datum.; DH
37.69290.Kurnakov and Voskresenskaya, 1936DH
40.440293.6Parks, Huffman, et al., 1933T = 92 to 294 K. Value is unsmoothed experimental datum.; DH

Phase change data

Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Reaction thermochemistry data, Gas phase ion energetics data, Ion clustering data, References, Notes

Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.

Data compiled as indicated in comments:
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, Chris Muzny director
BS - Robert L. Brown and Stephen E. Stein
AC - William E. Acree, Jr., James S. Chickos
DRB - Donald R. Burgess, Jr.
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
Tboil350.2 ± 0.2KAVGN/AAverage of 58 out of 72 values; Individual data points
Quantity Value Units Method Reference Comment
Tfus190. ± 1.KAVGN/AAverage of 6 values; Individual data points
Quantity Value Units Method Reference Comment
Ttriple189.3KN/AWilhoit, Chao, et al., 1985Uncertainty assigned by TRC = 0.05 K; TRC
Ttriple189.3KN/AParks, Huffman, et al., 1933, 2Uncertainty assigned by TRC = 0.2 K; TRC
Quantity Value Units Method Reference Comment
Tc530. ± 20.KAVGN/AAverage of 7 values; Individual data points
Quantity Value Units Method Reference Comment
Pc38.31atmN/AAmbrose, Ellender, et al., 1981Uncertainty assigned by TRC = 0.0382 atm; Visual; TRC
Pc37.80atmN/AYoung, 1910Uncertainty assigned by TRC = 0.8000 atm; TRC
Pc38.013atmN/AYoung and Thomas, 1893Uncertainty assigned by TRC = 0.39 atm; TRC
Pc39.65atmN/ANadezhdin, 1887Uncertainty assigned by TRC = 2.0000 atm; TRC
Pc42.24atmN/ASajots, 1879Uncertainty assigned by TRC = 4.000 atm; TRC
Quantity Value Units Method Reference Comment
ρc3.492mol/lN/AYoung, 1910Uncertainty assigned by TRC = 0.06 mol/l; TRC
ρc3.497mol/lN/AYoung and Thomas, 1893Uncertainty assigned by TRC = 0.05 mol/l; TRC
ρc3.397mol/lN/ANadezhdin, 1887Uncertainty assigned by TRC = 0.06 mol/l; TRC
Quantity Value Units Method Reference Comment
Δvap8.3 ± 0.4kcal/molAVGN/AAverage of 9 values; Individual data points

Enthalpy of vaporization

ΔvapH (kcal/mol) Temperature (K) Method Reference Comment
7.634350.3N/AMajer and Svoboda, 1985 
8.15315.N/AHernández and Ortega, 1997Based on data from 300. to 390. K.; AC
8.53303.AStephenson and Malanowski, 1987Based on data from 288. to 351. K. See also Polák and Mertl, 1965 and Dykyj, 1971.; AC
8.77286.N/AAmbrose, Ellender, et al., 1981, 2Based on data from 271. to 373. K. See also Boublik, Fried, et al., 1984.; AC
8.27 ± 0.02313.CSvoboda, Uchytilová, et al., 1980AC
7.50 ± 0.02343.CSvoboda, Uchytilová, et al., 1980AC
8.08 ± 0.02326.CSvoboda, Veselý, et al., 1977AC
7.98 ± 0.02331.CSvoboda, Veselý, et al., 1977AC
7.74 ± 0.02344.CSvoboda, Veselý, et al., 1977AC
7.62 ± 0.02351.CSvoboda, Veselý, et al., 1977AC
7.41 ± 0.02363.CSvoboda, Veselý, et al., 1977AC
8.13320.N/AConnett, Counsell, et al., 1976AC
7.62350.N/AConnett, Counsell, et al., 1976AC

Enthalpy of vaporization

ΔvapH = A exp(-βTr) (1 − Tr)β
    ΔvapH = Enthalpy of vaporization (at saturation pressure) (kcal/mol)
    Tr = reduced temperature (T / Tc)

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Temperature (K) A (kcal/mol) β Tc (K) Reference Comment
298. to 363.12.970.2982523.2Majer 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 Comment
288.73 to 348.984.222381245.702-55.189Polák and Mertl, 1965Coefficents calculated by NIST from author's data.

Enthalpy of fusion

ΔfusH (kcal/mol) Temperature (K) Reference Comment
2.505189.3Acree, 1991AC
2.5050189.3Parks, Huffman, et al., 1933DH

Entropy of fusion

ΔfusS (cal/mol*K) Temperature (K) Reference Comment
13.21189.3Parks, Huffman, et al., 1933DH

In addition to the Thermodynamics Research Center (TRC) data available from this site, much more physical and chemical property data is available from the following TRC products:


Reaction thermochemistry data

Go To: Top, Gas phase thermochemistry data, Condensed 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 as indicated in comments:
M - Michael M. Meot-Ner (Mautner) and Sharon G. Lias
B - John E. Bartmess
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.

Individual Reactions

C3H9Si+ + Ethyl Acetate = (C3H9Si+ • Ethyl Acetate)

By formula: C3H9Si+ + C4H8O2 = (C3H9Si+ • C4H8O2)

Quantity Value Units Method Reference Comment
Δr48.7kcal/molPHPMSWojtyniak and Stone, 1986gas phase; switching reaction,Thermochemical ladder((CH3)3Si+)H2O, Entropy change calculated or estimated; M
Quantity Value Units Method Reference Comment
Δr31.4cal/mol*KN/AWojtyniak and Stone, 1986gas phase; switching reaction,Thermochemical ladder((CH3)3Si+)H2O, Entropy change calculated or estimated; M

Free energy of reaction

ΔrG° (kcal/mol) T (K) Method Reference Comment
34.0468.PHPMSWojtyniak and Stone, 1986gas phase; switching reaction,Thermochemical ladder((CH3)3Si+)H2O, Entropy change calculated or estimated; M

C3H9Sn+ + Ethyl Acetate = (C3H9Sn+ • Ethyl Acetate)

By formula: C3H9Sn+ + C4H8O2 = (C3H9Sn+ • C4H8O2)

Quantity Value Units Method Reference Comment
Δr40.2kcal/molPHPMSStone and Splinter, 1984gas phase; switching reaction((CH3)3Sn+)CH3OH, Entropy change calculated or estimated; M
Quantity Value Units Method Reference Comment
Δr33.cal/mol*KN/AStone and Splinter, 1984gas phase; switching reaction((CH3)3Sn+)CH3OH, Entropy change calculated or estimated; M

Free energy of reaction

ΔrG° (kcal/mol) T (K) Method Reference Comment
22.9525.PHPMSStone and Splinter, 1984gas phase; switching reaction((CH3)3Sn+)CH3OH, Entropy change calculated or estimated; M

C4H7O2- + Hydrogen cation = Ethyl Acetate

By formula: C4H7O2- + H+ = C4H8O2

Quantity Value Units Method Reference Comment
Δr371.7 ± 4.1kcal/molG+TSHaas, Giblin, et al., 1998gas phase; From transesterification equilibria; B
Δr368.9 ± 1.2kcal/molEIAEMuftakhov, Vasil'ev, et al., 1999gas phase; B
Quantity Value Units Method Reference Comment
Δr365.0 ± 4.0kcal/molIMREHaas, Giblin, et al., 1998gas phase; From transesterification equilibria; B

C4H9O2+ + Ethyl Acetate = (C4H9O2+ • Ethyl Acetate)

By formula: C4H9O2+ + C4H8O2 = (C4H9O2+ • C4H8O2)

Bond type: Hydrogen bonds of the type OH-O between organics

Quantity Value Units Method Reference Comment
Δr29.2kcal/molPHPMSSzulejko and McMahon, 1991gas phase; M
Quantity Value Units Method Reference Comment
Δr34.6cal/mol*KPHPMSSzulejko and McMahon, 1991gas phase; M

Nitric oxide anion + Ethyl Acetate = (Nitric oxide anion • Ethyl Acetate)

By formula: NO- + C4H8O2 = (NO- • C4H8O2)

Quantity Value Units Method Reference Comment
Δr41.5kcal/molICRReents and Freiser, 1981gas phase; switching reaction,Thermochemical ladder(NO+)C2H5OH, Entropy change calculated or estimated; Farid and McMahon, 1978; M

Acetic acid ethenyl ester + Hydrogen = Ethyl Acetate

By formula: C4H6O2 + H2 = C4H8O2

Quantity Value Units Method Reference Comment
Δr-30.9 ± 1.1kcal/molChydVilcu and Perisanu, 1980liquid phase; ALS
Δr-31.12 ± 0.06kcal/molChydDolliver, Gresham, et al., 1938gas phase; At 355 °K; ALS

Acetylimidazole diethyl acetal + Water = Ethyl Acetate + 1H-Imidazole + Ethanol

By formula: C9H16N2O2 + H2O = C4H8O2 + C3H4N2 + C2H6O

Quantity Value Units Method Reference Comment
Δr-10.68 ± 0.16kcal/molCmGuthrie and Pike, 1987liquid phase; Heat of hydrolysis; ALS

Ethyl Acetate + Water = Ethanol + Acetic acid

By formula: C4H8O2 + H2O = C2H6O + C2H4O2

Quantity Value Units Method Reference Comment
Δr0.89 ± 0.04kcal/molCmWadso, 1958liquid phase; Heat of hydrolysis; ALS

Ethanol + Acetic acid = Ethyl Acetate + Water

By formula: C2H6O + C2H4O2 = C4H8O2 + H2O

Quantity Value Units Method Reference Comment
Δr3.97 ± 0.08kcal/molEqkHalford and Brundage, 1942gas phase; At 313 K; ALS

Hydrogen + Ethyl Acetate = 2Ethanol

By formula: H2 + C4H8O2 = 2C2H6O

Quantity Value Units Method Reference Comment
Δr-17.92 ± 0.13kcal/molCmWiberg, Crocker, et al., 1991liquid phase; ALS

Ketene + Ethanol = Ethyl Acetate

By formula: C2H2O + C2H6O = C4H8O2

Quantity Value Units Method Reference Comment
Δr-36.44kcal/molCmRice and Greenberg, 1934gas phase; ALS

Gas phase ion energetics data

Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry 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
MM - Michael M. Meot-Ner (Mautner)
LL - Sharon G. Lias and Joel F. Liebman
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 C4H8O2+ (ion structure unspecified)

Quantity Value Units Method Reference Comment
IE (evaluated)10.01 ± 0.05eVN/AN/AL
Quantity Value Units Method Reference Comment
Proton affinity (review)199.7kcal/molN/AHunter and Lias, 1998HL
Quantity Value Units Method Reference Comment
Gas basicity192.3kcal/molN/AHunter and Lias, 1998HL

Gas basicity at 298K

Gas basicity (review) (kcal/mol) Reference Comment
191.2 ± 0.05Decouzon, Gal, et al., 1996T = 338K; MM

Ionization energy determinations

IE (eV) Method Reference Comment
10.01 ± 0.05PIPECOFraser-Monteiro, Fraser-Monteiro, et al., 1982LBLHLM
10.0 ± 0.1CEMSJalonen, Tedder, et al., 1980LLK
10.16EIHolmes and Lossing, 1980LLK
9.90 ± 0.05PEBenoit, Harrison, et al., 1977LLK
10.24PESweigart and Turner, 1972LLK
10.11 ± 0.02PIWatanabe, Nakayama, et al., 1962RDSH
10.09 ± 0.02PIWatanabe, 1957RDSH
10.45PEJones, Modelli, et al., 1994Vertical value; LL
9.90PEBenoit and Harrison, 1977Vertical value; LLK

Appearance energy determinations

Ion AE (eV) Other Products MethodReferenceComment
CH3+13.94 ± 0.08?EIBrion and Dunning, 1963RDSH
C2H3+15.32 ± 0.20?EIFriedland and Strakna, 1956RDSH
C2H3O+11.0 ± 0.15C2H5OPIPECOFraser-Monteiro, Fraser-Monteiro, et al., 1982T = 298K; LBLHLM
C2H3O+11.7 ± 0.3C2H5OCEMSJalonen, Tedder, et al., 1980LLK
C2H3O+11.75 ± 0.07C2H5OEIBrion and Dunning, 1963RDSH
C2H3O2+11.74C2H5EIHolmes, Lossing, et al., 1991LL
C2H4O2+11.2 ± 0.1C2H4EIGodbole and Kebarle, 1962RDSH
C2H5+11.3 ± 0.1C2H3O2PIPECOFraser-Monteiro, Fraser-Monteiro, et al., 1982T = 298K; LBLHLM
C2H5+11.7 ± 0.3CH3COOCEMSJalonen, Tedder, et al., 1980LLK
C2H5+12.1?EITsuda and Hamill, 1966RDSH
C2H5O+10.7 ± 0.1C2H3OPIPECOFraser-Monteiro, Fraser-Monteiro, et al., 1982T = 298K; LBLHLM
C2H5O+10.7 ± 0.2CH3COCEMSJalonen, Tedder, et al., 1980LLK
C2H5O+10.8 ± 0.1CH3COEIMunson and Franklin, 1964RDSH
C2H5O2+10.62 ± 0.05C2H3EIHolmes and Lossing, 1984LBLHLM
C2H5O2+10.67 ± 0.08C2H3PIPECOFraser-Monteiro, Fraser-Monteiro, et al., 1982T = 298K; LBLHLM
C2H5O2+11.0 ± 0.1C2H3CEMSJalonen, Tedder, et al., 1980LLK
C2H5O2+10.6 ± 0.1C2H3EIBenoit, Harrison, et al., 1977LLK
C2H5O2+10.8 ± 0.1?EIHarrison and Jones, 1965RDSH
C3H5O2+10.6 ± 0.1CH3PIPECOFraser-Monteiro, Fraser-Monteiro, et al., 1982T = 298K; LBLHLM
C3H5O2+11.0 ± 0.1CH3EIGodbole and Kebarle, 1962RDSH
C4H6O+10.3 ± 0.1H2OPIPECOFraser-Monteiro, Fraser-Monteiro, et al., 1982T = 298K; LBLHLM
C4H6O+10.32 ± 0.05H2OEIHolmes, Burgers, et al., 1981LLK
C4H6O+10.45H2OEIBernecker and Long, 1961RDSH

De-protonation reactions

C4H7O2- + Hydrogen cation = Ethyl Acetate

By formula: C4H7O2- + H+ = C4H8O2

Quantity Value Units Method Reference Comment
Δr371.7 ± 4.1kcal/molG+TSHaas, Giblin, et al., 1998gas phase; From transesterification equilibria; B
Δr368.9 ± 1.2kcal/molEIAEMuftakhov, Vasil'ev, et al., 1999gas phase; B
Quantity Value Units Method Reference Comment
Δr365.0 ± 4.0kcal/molIMREHaas, Giblin, et al., 1998gas phase; From transesterification equilibria; B

Ion clustering data

Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry 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 by: 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

C3H9Si+ + Ethyl Acetate = (C3H9Si+ • Ethyl Acetate)

By formula: C3H9Si+ + C4H8O2 = (C3H9Si+ • C4H8O2)

Quantity Value Units Method Reference Comment
Δr48.7kcal/molPHPMSWojtyniak and Stone, 1986gas phase; switching reaction,Thermochemical ladder((CH3)3Si+)H2O, Entropy change calculated or estimated
Quantity Value Units Method Reference Comment
Δr31.4cal/mol*KN/AWojtyniak and Stone, 1986gas phase; switching reaction,Thermochemical ladder((CH3)3Si+)H2O, Entropy change calculated or estimated

Free energy of reaction

ΔrG° (kcal/mol) T (K) Method Reference Comment
34.0468.PHPMSWojtyniak and Stone, 1986gas phase; switching reaction,Thermochemical ladder((CH3)3Si+)H2O, Entropy change calculated or estimated

C3H9Sn+ + Ethyl Acetate = (C3H9Sn+ • Ethyl Acetate)

By formula: C3H9Sn+ + C4H8O2 = (C3H9Sn+ • C4H8O2)

Quantity Value Units Method Reference Comment
Δr40.2kcal/molPHPMSStone and Splinter, 1984gas phase; switching reaction((CH3)3Sn+)CH3OH, Entropy change calculated or estimated
Quantity Value Units Method Reference Comment
Δr33.cal/mol*KN/AStone and Splinter, 1984gas phase; switching reaction((CH3)3Sn+)CH3OH, Entropy change calculated or estimated

Free energy of reaction

ΔrG° (kcal/mol) T (K) Method Reference Comment
22.9525.PHPMSStone and Splinter, 1984gas phase; switching reaction((CH3)3Sn+)CH3OH, Entropy change calculated or estimated

C4H9O2+ + Ethyl Acetate = (C4H9O2+ • Ethyl Acetate)

By formula: C4H9O2+ + C4H8O2 = (C4H9O2+ • C4H8O2)

Bond type: Hydrogen bonds of the type OH-O between organics

Quantity Value Units Method Reference Comment
Δr29.2kcal/molPHPMSSzulejko and McMahon, 1991gas phase
Quantity Value Units Method Reference Comment
Δr34.6cal/mol*KPHPMSSzulejko and McMahon, 1991gas phase

Nitric oxide anion + Ethyl Acetate = (Nitric oxide anion • Ethyl Acetate)

By formula: NO- + C4H8O2 = (NO- • C4H8O2)

Quantity Value Units Method Reference Comment
Δr41.5kcal/molICRReents and Freiser, 1981gas phase; switching reaction,Thermochemical ladder(NO+)C2H5OH, Entropy change calculated or estimated; Farid and McMahon, 1978

References

Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry 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.

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]

Wiberg and Waldron, 1991
Wiberg, K.B.; Waldron, R.F., Lactones. 2. Enthalpies of hydrolysis, reduction, and formation of the C4-C13 monocyclic lactones. strain energies and conformations, J. Am. Chem. Soc., 1991, 113, 7697-7705. [all data]

Fenwick, Harrop, et al., 1978
Fenwick, J.O.; Harrop, D.; Head, A.J., Thermodynamic properties of organic oxygen compounds. 46. Enthalpies of formation of ethyl acetate and 1-hexanoix acid, J. Chem. Thermodyn., 1978, 10, 687-690. [all data]

Butwill and Rockenfeller, 1970
Butwill, M.E.; Rockenfeller, J.D., Heats of combustion and formation of ethyl acetate and isopropyl acetate, Thermochim. Acta, 1970, 1, 289-295. [all data]

Stull D.R., 1969
Stull D.R., Jr., The Chemical Thermodynamics of Organic Compounds. Wiley, New York, 1969. [all data]

Vvedenskii A.A., 1949
Vvedenskii A.A., Thermodynamics of the dehydrogenation reactions of alcohols. The equilibrium 2 C2H5OH = CH3COOC2H5 + 2 H2, Zh. Obshch. Khim., 1949, 19, 1094-1100. [all data]

Dorofeeva O.V., 1997
Dorofeeva O.V., Unpublished results. Thermocenter of Russian Academy of Science, Moscow, 1997. [all data]

Parks G.S., 1933
Parks G.S., Thermal data on organic compounds. XI. The heat capacities, entropies and free energies of ten compounds containing oxygen or nitrogen, J. Am. Chem. Soc., 1933, 55, 2733-2740. [all data]

Connett J.E., 1976
Connett J.E., Thermodynamic properties of organic oxygen compounds. XLIV. Vapor heat capacities and enthalpies of vaporization of methyl acetate, ethyl acetate, and propyl acetate, J. Chem. Thermodyn., 1976, 8, 1199-1203. [all data]

Bennewitz K., 1938
Bennewitz K., Molar heats of vapor organic compounds, Z. Phys. Chem. (Leipzig), 1938, B39, 126-144. [all data]

Jatkar S.K.K., 1939
Jatkar S.K.K., Supersonic velocity in gases and vapors. VI. Specific heats of the vapors of alcohols and ethyl acetate, J. Indian Inst. Sci., 1939, A22, 39-58. [all data]

Roth and Muller, 1929
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Notes

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