2,3-Butanedione
- Formula: C4H6O2
- Molecular weight: 86.0892
- IUPAC Standard InChIKey: QSJXEFYPDANLFS-UHFFFAOYSA-N
- CAS Registry Number: 431-03-8
- 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. - Species with the same structure:
- Other names: Biacetyl; Butane-2,3-dione; Butanedione; Diacetyl; Dimethyl diketone; Dimethyl glyoxal; 2,3-Butadione; 2,3-Diketobutane; (CH3CO)2; Glyoxal, dimethyl-; Butadione; UN 2346; 2,3-Dioxobutane; 2,3-Butandione; Buta-2,3-dione; Butan-2,3-dione; NSC 8750; butane-2,3-dione (diacetyl); 2,3-butanedione (diacetal); 2,3-butanedione (diacetyl); Butan-2,3-dione (diacetyl); Butanedione (diacetyl); 2,3 Butandione (Diacetyl); 2,3-butanodione
- Information on this page:
- Other data available:
- Data at other public NIST sites:
- Options:
Data at NIST subscription sites:
NIST subscription sites provide data under the NIST Standard Reference Data Program, but require an annual fee to access. The purpose of the fee is to recover costs associated with the development of data collections included in such sites. Your institution may already be a subscriber. Follow the links above to find out more about the data in these sites and their terms of usage.
Gas phase thermochemistry data
Go To: Top, Condensed phase thermochemistry data, 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: Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°gas | -78.10 | kcal/mol | Ccb | Nicholson, Szwarc, et al., 1954 |
Condensed phase thermochemistry data
Go To: Top, Gas phase thermochemistry data, 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: Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°liquid | -87.35 | kcal/mol | Ccb | Nicholson, Szwarc, et al., 1954 | |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -493.81 ± 0.19 | kcal/mol | Ccb | Nicholson, Szwarc, et al., 1954 | Corresponding ΔfHºliquid = -87.34 kcal/mol (simple calculation by NIST; no Washburn corrections) |
Phase change data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry 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 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
AC - William E. Acree, Jr., James S. Chickos
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 361.2 | K | N/A | Weast and Grasselli, 1989 | BS |
Tboil | 361.15 | K | N/A | Othmer, 1943 | Uncertainty assigned by TRC = 1. K; TRC |
Tboil | 361.15 | K | N/A | Sabatier and Mailhe, 1909 | Uncertainty assigned by TRC = 2. K; TRC |
Tboil | 360.15 | K | N/A | Sabatier and Mailhe, 1907 | Uncertainty assigned by TRC = 2. K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 9.25 ± 0.22 | kcal/mol | V | Nicholson, Szwarc, et al., 1954 | ALS |
Enthalpy of vaporization
ΔvapH (kcal/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
9.20 | 288. | A,I | Stephenson and Malanowski, 1987 | Based on data from 273. to 348. K. See also Neely and Hall, 1972.; AC |
9.46 ± 0.05 | 283. | N/A | Nicholson, Szwarc, et al., 1954, 2 | Based on data from 273. to 293. K.; AC |
Antoine Equation Parameters
log10(P) = A − (B / (T + C))
P = vapor pressure (atm)
T = temperature (K)
View plot Requires a JavaScript / HTML 5 canvas capable browser.
Temperature (K) | A | B | C | Reference | Comment |
---|---|---|---|---|---|
273.16 to 348.16 | 3.53347 | 927.108 | -98.949 | Neely and Hall, 1972 | Coefficents calculated by NIST from author's data. |
Henry's Law data
Go To: Top, Gas phase thermochemistry data, Condensed 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 | Comment |
---|---|---|---|---|
74. | 5700. | M | N/A | |
57. | M | N/A | ||
190. | X | N/A | Value given here as quoted by missing citation. |
References
Go To: Top, Gas phase thermochemistry data, Condensed 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.
Nicholson, Szwarc, et al., 1954
Nicholson, G.R.; Szwarc, M.; Taylor, J.W.,
The heats of formation of diacetyl and of benzyl methyl ketone in the vapour phase,
J. Chem. Soc., 1954, 2767-2769. [all data]
Weast and Grasselli, 1989
CRC Handbook of Data on Organic Compounds, 2nd Editon, Weast,R.C and Grasselli, J.G., ed(s)., CRC Press, Inc., Boca Raton, FL, 1989, 1. [all data]
Othmer, 1943
Othmer, D.F.,
Composition of vapors from boiling binary solutions,
Ind. Eng. Chem., 1943, 35, 614-20. [all data]
Sabatier and Mailhe, 1909
Sabatier, P.; Mailhe, A.,
New Applications of the General Method of Hydrogenation with Various Metals,
Ann. Chim. Phys., 1909, 16, 70. [all data]
Sabatier and Mailhe, 1907
Sabatier, P.; Mailhe, A.,
The Direct Hydrogenation of Methyl Diketones,
C. R. Hebd. Seances Acad. Sci., 1907, 144, 1086. [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]
Neely and Hall, 1972
Neely, William C.; Hall, Terry D.,
Vapor pressure of biacetyl,
J. Chem. Eng. Data, 1972, 17, 3, 294-295, https://doi.org/10.1021/je60054a010
. [all data]
Nicholson, Szwarc, et al., 1954, 2
Nicholson, G.R.; Szwarc, M.; Taylor, J. Watson,
The heats of formation of diacetyl and of benzyl methyl ketone in the vapour phase,
J. Chem. Soc., 1954, 2767, https://doi.org/10.1039/jr9540002767
. [all data]
Notes
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Henry's Law data, References
- Symbols used in this document:
Tboil Boiling 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 ΔvapH Enthalpy of vaporization ΔvapH° Enthalpy of vaporization at standard conditions - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
- The National Institute of Standards and Technology (NIST) uses its best efforts to deliver a high quality copy of the Database and to verify that the data contained therein have been selected on the basis of sound scientific judgment. However, NIST makes no warranties to that effect, and NIST shall not be liable for any damage that may result from errors or omissions in the Database.
- Customer support for NIST Standard Reference Data products.