Methyl formate
- Formula: C2H4O2
- Molecular weight: 60.0520
- IUPAC Standard InChIKey: TZIHFWKZFHZASV-UHFFFAOYSA-N
- CAS Registry Number: 107-31-3
- 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: Formic acid, methyl ester; Methyl methanoate; HCOOCH3; Formiate de methyle; Methylester kyseliny mravenci; Methylformiaat; Methylformiat; Mravencan methylnaty; UN 1243; Methyl ester of formic acid; Methanoic acid methyl ester
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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, Gas phase ion energetics 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 as indicated in comments:
DRB - Donald R. Burgess, Jr.
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 | -80.52 | kcal/mol | N/A | Gladii, Starchevskii, et al., 1990 | Value computed using ΔfHliquid° value of -365.9 kj/mol from Gladii, Starchevskii, et al., 1990 and ΔvapH° value of 29.0 kj/mol from Hine and Klueppet, 1974.; DRB |
ΔfH°gas | -83.41 | kcal/mol | N/A | Guthrie, 1974 | Value computed using ΔfHliquid° value of -378.0 kj/mol from Guthrie, 1974 and ΔvapH° value of 29.0 kj/mol from Hine and Klueppet, 1974.; DRB |
ΔfH°gas | -86.6 | kcal/mol | Cm | Hine and Klueppet, 1974 | ALS |
ΔfH°gas | -84.97 | kcal/mol | Ccr | Hall and Baldt, 1971 | ALS |
Constant pressure heat capacity of gas
Cp,gas (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
10.53 | 100. | Chao J., 1986 | p=1 bar. Recommended S(T) and Cp(T) values are in close agreement with statistical values calculated by [ Vay P.-M., 1971] (discrepancies in S(T) do not exceed 1.3 J/mol*K) and value of S(298.15 K)=286.10 J/mol*K determined from high accuracy ab initio calculation [ East A.L.L., 1997].; GT |
11.91 | 150. | ||
12.95 | 200. | ||
14.69 | 273.15 | ||
15.39 ± 0.02 | 298.15 | ||
15.44 | 300. | ||
18.54 | 400. | ||
21.58 | 500. | ||
24.276 | 600. | ||
26.592 | 700. | ||
28.568 | 800. | ||
30.261 | 900. | ||
31.711 | 1000. | ||
32.957 | 1100. | ||
34.030 | 1200. | ||
34.952 | 1300. | ||
35.750 | 1400. | ||
36.444 | 1500. |
Condensed phase thermochemistry 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:
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 | -87.45 | kcal/mol | Eqk | Gladii, Starchevskii, et al., 1990 | ALS |
ΔfH°liquid | -90.35 | kcal/mol | Cm | Guthrie, 1974 | Heat of hydrolysis; ALS |
ΔfH°liquid | -93.4 | kcal/mol | Cm | Hine and Klueppet, 1974 | ALS |
ΔfH°liquid | -92.28 | kcal/mol | Ccr | Hall and Baldt, 1971 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -232.46 ± 0.14 | kcal/mol | Ccr | Hall and Baldt, 1971 | Corresponding ΔfHºliquid = -92.27 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS |
Constant pressure heat capacity of liquid
Cp,liquid (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
28.817 | 298.75 | Zabransky, Hynek, et al., 1987 | T = 293 to 299 K. Unsmoothed experimental datum.; DH |
28.61 | 298.15 | Fuchs, 1979 | DH |
22.8 | 297. | Hall and Baldt, 1971 | DH |
28.99 | 288. | Mehl, 1934 | DH |
31.1 | 298. | Berthelot and Ogier, 1881 | T = 286 to 302 K. Cp given as 0.516 cal/g*K.; 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
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
DRB - Donald R. Burgess, Jr.
AC - William E. Acree, Jr., James S. Chickos
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 305. ± 1. | K | AVG | N/A | Average of 20 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 173.2 | K | N/A | Timmermans, 1935 | Uncertainty assigned by TRC = 2. K; TRC |
Tfus | 173.4 | K | N/A | Timmermans, 1911 | Uncertainty assigned by TRC = 0.3 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 487.2 | K | N/A | Majer and Svoboda, 1985 | |
Tc | 487.2 | K | N/A | Young, 1910 | Uncertainty assigned by TRC = 1. K; TRC |
Tc | 487.2 | K | N/A | Young and Thomas, 1893 | Uncertainty assigned by TRC = 1. K; TRC |
Tc | 523.7 | K | N/A | De Heen, 1888 | Uncertainty assigned by TRC = 20. K; TRC |
Tc | 485.2 | K | N/A | Nadezhdin, 1887 | Uncertainty assigned by TRC = 2. K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 59.25 | atm | N/A | Young, 1910 | Uncertainty assigned by TRC = 0.6000 atm; TRC |
Pc | 59.289 | atm | N/A | Young and Thomas, 1893 | Uncertainty assigned by TRC = 0.39 atm; TRC |
Pc | 61.65 | atm | N/A | Nadezhdin, 1887 | Uncertainty assigned by TRC = 2.0000 atm; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 5.818 | mol/l | N/A | Young, 1910 | Uncertainty assigned by TRC = 0.08 mol/l; TRC |
ρc | 5.818 | mol/l | N/A | Young and Thomas, 1893 | Uncertainty assigned by TRC = 0.07 mol/l; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 7.0 ± 0.5 | kcal/mol | AVG | N/A | Average of 6 values; Individual data points |
Enthalpy of vaporization
ΔvapH (kcal/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
6.673 | 304.7 | N/A | Majer and Svoboda, 1985 | |
7.07 | 292. | A | Stephenson and Malanowski, 1987 | Based on data from 279. to 305. K.; AC |
6.79 | 320. | A | Stephenson and Malanowski, 1987 | Based on data from 305. to 443. K.; AC |
6.86 ± 0.02 | 293. | C | Cihlár, Hynek, et al., 1976 | AC |
6.67 ± 0.02 | 305. | C | Cihlár, Hynek, et al., 1976 | AC |
6.55 ± 0.02 | 313. | C | Cihlár, Hynek, et al., 1976 | AC |
7.19 | 283. | BG | Baldt and Hall, 1971 | Based on data from 261. to 305. K.; AC |
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 |
---|---|---|---|---|---|
293. to 314. | 11.02 | 0.3119 | 487.2 | 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 | Comment |
---|---|---|---|---|---|
294. to 304.9 | 0.24526 | 6.524 | -278.54 | Nelson, 1928 | Coefficents calculated by NIST from author's data. |
Reaction thermochemistry 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:
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
C2H3O2- + =
By formula: C2H3O2- + H+ = C2H4O2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | <384.00 | kcal/mol | CIDT | Graul and Squires, 1988 | gas phase; B |
ΔrH° | <391.75 ± 0.90 | kcal/mol | G+TS | DePuy, Grabowski, et al., 1985 | gas phase; HO- + DCO2CH3 -> (M-D)-. ΔHf(MeO- + CO) = -59.7 kcal/mol; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | <384.00 | kcal/mol | IMRB | DePuy, Grabowski, et al., 1985 | gas phase; HO- + DCO2CH3 -> (M-D)-. ΔHf(MeO- + CO) = -59.7 kcal/mol; B |
C2H3O2- + =
By formula: C2H3O2- + H+ = C2H4O2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 391.2 ± 4.1 | kcal/mol | G+TS | DePuy, Grabowski, et al., 1985 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 384.1 ± 4.0 | kcal/mol | IMRB | DePuy, Grabowski, et al., 1985 | gas phase; B |
By formula: C4H10O3 + H2O = C2H4O2 + 2CH4O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -2.29 ± 0.28 | kcal/mol | Cm | Hine and Klueppet, 1974 | liquid phase; 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 |
---|---|---|---|---|
4.1 | M | N/A | ||
4.5 | Q | N/A | missing citation is quoted as the source. However, there only activity coefficients and no vapor pressures are listed. | |
4.5 | Q | N/A | missing citation is quoted as the source. However, there only activity coefficients and no vapor pressures are listed. | |
4.1 | 3800. | M | N/A |
Gas phase ion energetics data
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 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
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 C2H4O2+ (ion structure unspecified)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
IE (evaluated) | 10.835 | eV | N/A | N/A | L |
Quantity | Value | Units | Method | Reference | Comment |
Proton affinity (review) | 187.0 | kcal/mol | N/A | Hunter and Lias, 1998 | HL |
Quantity | Value | Units | Method | Reference | Comment |
Gas basicity | 179.6 | kcal/mol | N/A | Hunter and Lias, 1998 | HL |
Ionization energy determinations
IE (eV) | Method | Reference | Comment |
---|---|---|---|
10.835 | TE | Waterstradt, Jung, et al., 1994 | LL |
~10.7 | PE | Cannington and Ham, 1985 | LBLHLM |
10.99 | PE | Kimura, Katsumata, et al., 1981 | LLK |
10.85 ± 0.05 | PE | Benoit, Harrison, et al., 1977 | LLK |
10.85 | PE | Sweigart and Turner, 1972 | LLK |
10.815 ± 0.005 | PI | Watanabe, Nakayama, et al., 1962 | RDSH |
11.0 | PE | Cannington and Ham, 1985 | Vertical value; LBLHLM |
10.85 | PE | Benoit and Harrison, 1977 | Vertical value; LLK |
10.3 | PE | Rao, 1975 | Vertical value; LLK |
Appearance energy determinations
Ion | AE (eV) | Other Products | Method | Reference | Comment |
---|---|---|---|---|---|
CHO+ | 12.91 ± 0.07 | CH3O | PIPECO | Nishimura, Zha, et al., 1987 | LBLHLM |
CHO+ | 13.47 ± 0.05 | CH3O | EI | Haney and Franklin, 1969 | RDSH |
CHO2+ | 15.9 | CH3 | EI | King and Long, 1958 | RDSH |
CH2+ | 19.8 | ? | EI | King and Long, 1958 | RDSH |
CH2O+ | 13.6 | ? | EI | King and Long, 1958 | RDSH |
CH3+ | 13.27 ± 0.24 | HCO2 | PIPECO | Nishimura, Zha, et al., 1987 | LBLHLM |
CH3+ | 13.71 | ? | EI | Haney and Franklin, 1969 | RDSH |
CH3O+ | 12.23 | CHO | EI | Haney and Franklin, 1969 | RDSH |
CH4O+ | 11.47 ± 0.05 | CO | PIPECO | Nishimura, Zha, et al., 1987 | LBLHLM |
CH4O+ | 11.5 ± 0.1 | CO | EI | VanRaalte and Harrison, 1963 | RDSH |
C2H3O2+ | 12.3 | H | EI | King and Long, 1958 | RDSH |
De-protonation reactions
C2H3O2- + =
By formula: C2H3O2- + H+ = C2H4O2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | <384.00 | kcal/mol | CIDT | Graul and Squires, 1988 | gas phase; B |
ΔrH° | <391.75 ± 0.90 | kcal/mol | G+TS | DePuy, Grabowski, et al., 1985 | gas phase; HO- + DCO2CH3 -> (M-D)-. ΔHf(MeO- + CO) = -59.7 kcal/mol; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | <384.00 | kcal/mol | IMRB | DePuy, Grabowski, et al., 1985 | gas phase; HO- + DCO2CH3 -> (M-D)-. ΔHf(MeO- + CO) = -59.7 kcal/mol; B |
C2H3O2- + =
By formula: C2H3O2- + H+ = C2H4O2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 391.2 ± 4.1 | kcal/mol | G+TS | DePuy, Grabowski, et al., 1985 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 384.1 ± 4.0 | kcal/mol | IMRB | DePuy, Grabowski, et al., 1985 | gas phase; B |
IR Spectrum
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Data compiled by: Coblentz Society, Inc.
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
View image of digitized spectrum (can be printed in landscape orientation).
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-3741 |
NIST MS number | 228212 |
Vibrational and/or electronic energy levels
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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: 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 | CH3 d-str | 3045 | D | 3045 M | gas | 3030 | liq. | ||
a' | 2 | CH3 s-str | 2969 | D | 2969 S | gas | 2955 p | liq. | ||
a' | 3 | CH str | 2943 | D | 2943 S | gas | ||||
a' | 4 | C=O str | 1754 | C | 1754 VS | gas | 1717 p | liq. | ||
a' | 5 | CH3 d-deform | 1454 | D | 1454 W | solid solid | ||||
a' | 6 | CH3 s-deform | 1445 | D | 1445 M | gas | ||||
a' | 7 | CH bend | 1371 | D | 1371 W | gas | 1379 p | liq. | ||
a' | 8 | C-O str | 1207 | C | 1207 VS | gas | 1207 | liq. | ||
a' | 9 | CH3 rock | 1166 | D | 1166 VS | gas | 1157 | liq. | ||
a' | 10 | O-CH3 str | 925 | C | 925 S | gas | 912 p | liq. | ||
a' | 11 | OCO deform | 767 | C | 767 M | gas | 765 | liq. | ||
a' | 12 | COC deform | 318 | D | 318 M | gas | ||||
a | 13 | CH3 d-str | 3012 | D | 3012 M | gas | ||||
a | 14 | CH3 d-deform | 1443 | E | 1443 W | solid solid | 1440 | liq. | ||
a | 15 | CH3 rock | 1168 | D | 1168 M | gas | ||||
a | 16 | CH bend | 1032 | C | 1032 M | gas | 1030 | liq. | ||
a | 17 | C-O torsion | 332 | D | 332 M | gas | 332 p | liq. | ||
a | 18 | CH3 torsion | 130 | D | 130 VW | gas | MW: ν132 | |||
Source: Shimanouchi, 1972
Notes
VS | Very strong |
S | Strong |
M | Medium |
W | Weak |
VW | Very weak |
p | Polarized |
MW | Torsional Frequency calculated from microwave spectroscopic data. |
C | 3~6 cm-1 uncertainty |
D | 6~15 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, Gas phase ion energetics data, IR Spectrum, Mass spectrum (electron ionization), 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.
Gladii, Starchevskii, et al., 1990
Gladii, S.L.; Starchevskii, M.K.; Pazderskii, Yu.A.; Moiseev, I.I.,
Chemical equilibrium in the methyl formate-water-methanol-formic acid system,
J. Appl. Chem. USSR, 1990, 63, 106-111. [all data]
Hine and Klueppet, 1974
Hine, J.; Klueppet, A.W.,
Structural effects on rates and equilibria. XVIII. Thermodynamic stability of ortho esters,
J. Am. Chem. Soc., 1974, 96, 2924-2929. [all data]
Guthrie, 1974
Guthrie, J.P.,
Hydration of carboxamides. Evaluation of the free energy change for addition of water to acetamide and formamide derivatives,
J. Am. Chem. Soc., 1974, 96, 3608-3615. [all data]
Hall and Baldt, 1971
Hall, H.K., Jr.; Baldt, J.H.,
Thermochemistry of strained-ring bridgehead nitriles and esters,
J. Am. Chem. Soc., 1971, 93, 140-145. [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]
Vay P.-M., 1971
Vay P.-M.,
Tables of thermodynamic functions for gaseous methyl formate and methyl acetate,
J. Chim. Phys. Physico-Chim. Biol., 1971, 68, 1757-1758. [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]
Zabransky, Hynek, et al., 1987
Zabransky, M.; Hynek, V.; Finkeova-Hastabova, J.; Vesely, F.,
Heat capacities of six liquid esters as a function of temperature,
Coll. Czech. Chem. Comm., 1987, 52, 251-256. [all data]
Fuchs, 1979
Fuchs, R.,
Heat capacities of some liquid aliphatic, alicyclic, and aromatic esters at 298.15 K,
J. Chem. Thermodyn., 1979, 11, 959-961. [all data]
Mehl, 1934
Mehl, W.,
Die spezifische Wärme einiger flüssiger Kältemittel,
Z. ges. Kalte-Ind., 1934, 41, 152-153. [all data]
Berthelot and Ogier, 1881
Berthelot, M.; Ogier, J.,
Recherches sur les ethers formiques,
Ann. chim. et phys., 1881, 23(5), 201-209. [all data]
Timmermans, 1935
Timmermans, J.,
Researches in Stoichiometry. I. The Heat of Fusion of Organic Compounds.,
Bull. Soc. Chim. Belg., 1935, 44, 17-40. [all data]
Timmermans, 1911
Timmermans, J.,
Researches on the freezing point of organic liquid compounds,
Bull. Soc. Chim. Belg., 1911, 25, 300. [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]
Young, 1910
Young, S.,
The Internal Heat of Vaporization constants of thirty pure substances,
Sci. Proc. R. Dublin Soc., 1910, 12, 374. [all data]
Young and Thomas, 1893
Young, S.; Thomas, G.L.,
The vapour pressures, molecular volumes, and critical constants of ten of the lower esters,
J. Chem. Soc., 1893, 63, 1191. [all data]
De Heen, 1888
De Heen, P.,
Research on Physics and Theory of Liquids, Experimental Part Paris, 1888. [all data]
Nadezhdin, 1887
Nadezhdin, A.,
Rep. Phys., 1887, 23, 708. [all data]
Stephenson and Malanowski, 1987
Stephenson, Richard M.; Malanowski, Stanislaw,
Handbook of the Thermodynamics of Organic Compounds, 1987, https://doi.org/10.1007/978-94-009-3173-2
. [all data]
Cihlár, Hynek, et al., 1976
Cihlár, J.; Hynek, V.; Svoboda, V.; Holub, R.,
Heats of vaporization of alkyl esters of formic acid,
Collect. Czech. Chem. Commun., 1976, 41, 1, 1-6, https://doi.org/10.1135/cccc19760001
. [all data]
Baldt and Hall, 1971
Baldt, J.H.; Hall, H.K.K., Jr.,
Thermochemistry of strained-ring bridgehead nitriles and esters,
J. Am. Chem. Soc., 1971, 93, 140-145. [all data]
Nelson, 1928
Nelson, O.A.,
Vapor Pressures of Fumigants: II---Methyl, Ethyl, n-Propyl, Isopropyl, n-Butyl, Secondary Butyl and Isobutyl Formates 1,
Ind. Eng. Chem., 1928, 20, 12, 1382-1384, https://doi.org/10.1021/ie50228a035
. [all data]
Graul and Squires, 1988
Graul, S.T.; Squires, R.R.,
On the Existence of Alkyl Carbanions in the Gas Phase,
J. Am. Chem. Soc., 1988, 110, 2, 607, https://doi.org/10.1021/ja00210a054
. [all data]
DePuy, Grabowski, et al., 1985
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Notes
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- Symbols used in this document:
AE Appearance energy Cp,gas Constant pressure heat capacity of gas Cp,liquid Constant pressure heat capacity of liquid IE (evaluated) Recommended ionization energy Pc Critical pressure 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 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 ΔrG° Free energy of reaction at standard conditions ΔrH° Enthalpy 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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