Acetic acid, butyl ester
- Formula: C6H12O2
- Molecular weight: 116.1583
- IUPAC Standard InChIKey: DKPFZGUDAPQIHT-UHFFFAOYSA-N
- CAS Registry Number: 123-86-4
- 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: n-Butyl acetate; Butyl acetate; Butyl ethanoate; 1-Butyl acetate; CH3COO(CH2)3CH3; Acetic acid n-butyl ester; n-Butyl ethanoate; Acetate de butyle; Butile(acetati di); Butylacetat; Butylacetaten; Butyle (acetate de); Butylester kyseliny octove; Butyl ester of acetic acid; 1-Acetoxybutane; 1-Butanol, acetate; Butyl ester, acetic acid; NSC 9298; Butile; Butyle; UN 1123
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Gas phase thermochemistry data
Go To: Top, Phase change data, Henry's Law 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: Donald R. Burgess, Jr.
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°gas | -135.3 | kcal/mol | N/A | Schiopu, Bot, et al., 1961 | Value computed using ΔfHliquid° value of -609.6 kj/mol from Schiopu, Bot, et al., 1961 and ΔvapH° value of 43.6±0.2 kj/mol from missing citation. |
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:
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
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 399. ± 1. | K | AVG | N/A | Average of 21 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 196.35 | K | N/A | Timmermans, 1921 | Uncertainty assigned by TRC = 0.3 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 196.03 | K | N/A | Balakina, Petrova, et al., 1979 | Uncertainty assigned by TRC = 0.1 K; TRC |
Ttriple | 196.12 | K | N/A | Balakina, Petrova, et al., 1979 | Uncertainty assigned by TRC = 0.05 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 575.4 | K | N/A | Quadri and Kudchadker, 1991 | Uncertainty assigned by TRC = 0.6 K; TRC |
Tc | 579. | K | N/A | Majer and Svoboda, 1985 | |
Tc | 560.2 | K | N/A | De Heen, 1888 | Uncertainty assigned by TRC = 10. K; TRC |
Tc | 561. | K | N/A | Nadezhdin, 1887 | Uncertainty assigned by TRC = 10. K; TRC |
Tc | 579.1 | K | N/A | Pawlewski, 1882 | Uncertainty assigned by TRC = 3. K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 30.50 | atm | N/A | Quadri and Kudchadker, 1991 | Uncertainty assigned by TRC = 0.20 atm; TRC |
Pc | 30.59 | atm | N/A | Nadezhdin, 1887 | Uncertainty assigned by TRC = 0.99995 atm; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 10.2 ± 0.9 | kcal/mol | AVG | N/A | Average of 10 values; Individual data points |
Enthalpy of vaporization
ΔvapH (kcal/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
8.671 | 399.2 | N/A | Majer and Svoboda, 1985 | |
9.68 | 356. | A,EB | Stephenson and Malanowski, 1987 | Based on data from 341. to 399. K. See also Sheehan and Langer, 1969.; AC |
9.75 | 347. | A | Stephenson and Malanowski, 1987 | Based on data from 332. to 399. K. See also Kliment, Fried, et al., 1964 and Boublik, Fried, et al., 1984.; AC |
9.87 | 341. | DTA | Meyer, Awe, et al., 1980 | Based on data from 326. to 404. K.; AC |
10.3 ± 0.02 | 313. | C | Svoboda, Uchytilová, et al., 1980 | AC |
9.97 ± 0.02 | 328. | C | Svoboda, Uchytilová, et al., 1980 | AC |
9.70 ± 0.02 | 343. | C | Svoboda, Uchytilová, et al., 1980 | AC |
9.42 ± 0.02 | 358. | C | Svoboda, Uchytilová, et al., 1980 | AC |
8.96 | 398. | N/A | Schiopu, Bot, et al., 1961, 2 | 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 |
---|---|---|---|---|---|
298. to 358. | 15.31 | 0.306 | 579. | 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 |
---|---|---|---|---|---|
332.89 to 399.24 | 4.26232 | 1440.231 | -61.362 | Kliment, Fried, et al., 1964 | Coefficents calculated by NIST from author's data. |
Henry's Law data
Go To: Top, Gas phase thermochemistry data, Phase change data, References, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data compiled by: Rolf Sander
Henry's Law constant (water solution)
kH(T) = k°H exp(d(ln(kH))/d(1/T) ((1/T) - 1/(298.15 K)))
k°H = Henry's law constant for solubility in water at 298.15 K (mol/(kg*bar))
d(ln(kH))/d(1/T) = Temperature dependence constant (K)
k°H (mol/(kg*bar)) | d(ln(kH))/d(1/T) (K) | Method | Reference |
---|---|---|---|
3.5 | X | N/A | |
3.5 | 7500. | X | N/A |
2.1 | 3200. | X | N/A |
3.6 | 6000. | M | N/A |
3.0 | V | N/A |
References
Go To: Top, Gas phase thermochemistry data, Phase change data, Henry's Law data, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Schiopu, Bot, et al., 1961
Schiopu, M.; Bot, O.; Onu, V.,
Studiul termodinamic si cinetic al sistemului acetat de n-butil-apa. Nota I.,
Bul. Inst. Poleteh. Iasi, 1961, 7, 115-118. [all data]
Timmermans, 1921
Timmermans, J.,
The Freezing Points of Organic Substances IV. New Exp. Determinations,
Bull. Soc. Chim. Belg., 1921, 30, 62. [all data]
Balakina, Petrova, et al., 1979
Balakina, M.M.; Petrova, G.V.; Vasil'ev, I.A.,
Heat capacity of butyl acetate and butyl Butyrate in a liquid state.,
Termodin. Org. Soedin., 1979, No. 8, 37. [all data]
Quadri and Kudchadker, 1991
Quadri, S.K.; Kudchadker, A.P.,
Measurement of the critical temperatures and critical pressures of some thermally stable or mildly unstable esters, ketones, and ethers,
J. Chem. Thermodyn., 1991, 23, 129-34. [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]
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]
Pawlewski, 1882
Pawlewski, B.,
The critical temperatures of ester compounds,
Ber. Dtsch. Chem. Ges., 1882, 15, 2460-4. [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]
Sheehan and Langer, 1969
Sheehan, Richard J.; Langer, Stanley H.,
Vapor pressures of fluorine- and silicon-containing derivatives of some hydroxylic compounds,
J. Chem. Eng. Data, 1969, 14, 2, 248-250, https://doi.org/10.1021/je60041a011
. [all data]
Kliment, Fried, et al., 1964
Kliment, V.; Fried, V.; Pick, J.,
Gleichgewicht flüssigkeit-dampf XXXIII. Systeme butylacetat-phenol und wasser-phenol,
Collect. Czech. Chem. Commun., 1964, 29, 9, 2008-2015, https://doi.org/10.1135/cccc19642008
. [all data]
Boublik, Fried, et al., 1984
Boublik, T.; Fried, V.; Hala, E.,
The Vapour Pressures of Pure Substances: Selected Values of the Temperature Dependence of the Vapour Pressures of Some Pure Substances in the Normal and Low Pressure Region, 2nd ed., Elsevier, New York, 1984, 972. [all data]
Meyer, Awe, et al., 1980
Meyer, Edwin F.; Awe, Michael J.; Wagner, Robert E.,
Cohesive energies in polar organic liquids. 4. n-Alkyl acetates,
J. Chem. Eng. Data, 1980, 25, 4, 371-374, https://doi.org/10.1021/je60087a030
. [all data]
Svoboda, Uchytilová, et al., 1980
Svoboda, Václav; Uchytilová, Vera; Majer, Vladimír; Pick, Jirí,
Heats of vaporization of alkyl esters of formic, acetic and propionic acids,
Collect. Czech. Chem. Commun., 1980, 45, 12, 3233-3240, https://doi.org/10.1135/cccc19803233
. [all data]
Schiopu, Bot, et al., 1961, 2
Schiopu, I.M.; Bot, O.; Onu, V.,
Bull. Inst. Politeh. Iasi., 1961, 7, 115. [all data]
Notes
Go To: Top, Gas phase thermochemistry data, Phase change data, Henry's Law data, References
- Symbols used in this document:
Pc Critical pressure 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 ΔfH°gas Enthalpy of formation of gas at standard conditions ΔvapH Enthalpy of vaporization ΔvapH° Enthalpy of vaporization at standard conditions - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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