1,2-Butadiene
- Formula: C4H6
- Molecular weight: 54.0904
- IUPAC Standard InChIKey: QNRMTGGDHLBXQZ-UHFFFAOYSA-N
- CAS Registry Number: 590-19-2
- 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: Allene, methyl-; Methylallene; CH2=C=CHCH3; Buta-1,2-diene
- Permanent link for this species. Use this link for bookmarking this species for future reference.
- 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, 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 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 | 162.2 ± 0.59 | kJ/mol | Cm | Prosen, Maron, et al., 1951 | ALS |
ΔfH°gas | 165.4 ± 1.2 | kJ/mol | Ccb | Prosen, Maron, et al., 1949 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°gas | -2593.8 ± 0.54 | kJ/mol | Cm | Prosen, Maron, et al., 1951 | Corresponding ΔfHºgas = 162.3 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°gas | -2597.0 ± 1.2 | kJ/mol | Ccb | Prosen, Maron, et al., 1949 | Corresponding ΔfHºgas = 165.4 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
35.83 | 50. | Thermodynamics Research Center, 1997 | Recommended values are in close agreement with those obtained from earlier statistical thermodynamics calculation [ Kilpatrick J.E., 1949].; GT |
45.63 | 100. | ||
54.41 | 150. | ||
62.51 | 200. | ||
75.00 | 273.15 | ||
79.48 | 298.15 | ||
79.81 | 300. | ||
97.62 | 400. | ||
113.74 | 500. | ||
127.62 | 600. | ||
139.54 | 700. | ||
149.8 | 800. | ||
159.8 | 900. | ||
166.5 | 1000. | ||
173.3 | 1100. | ||
179.1 | 1200. | ||
184.2 | 1300. | ||
188.6 | 1400. | ||
192.4 | 1500. |
Phase change data
Go To: Top, Gas phase thermochemistry 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
AC - William E. Acree, Jr., James S. Chickos
DH - Eugene S. Domalski and Elizabeth D. Hearing
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 284. | K | N/A | Majer and Svoboda, 1985 | |
Tboil | 291.7 | K | N/A | Feugeas and Giusti, 1968 | Uncertainty assigned by TRC = 2. K; TRC |
Tboil | 284.06 | K | N/A | Streiff, Murphy, et al., 1946 | Uncertainty assigned by TRC = 0.3 K; TRC |
Tboil | 283.5 | K | N/A | Hurd and Meinert, 1931 | Uncertainty assigned by TRC = 0.5 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 136.940 | K | N/A | Streiff, Murphy, et al., 1947 | Uncertainty assigned by TRC = 0.05 K; TRC |
Tfus | 136.960 | K | N/A | Streiff, Murphy, et al., 1947 | Uncertainty assigned by TRC = 0.02 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 136.920 | K | N/A | Aston and Szasz, 1947 | Uncertainty assigned by TRC = 0.06 K; TRC |
Ttriple | 136.950 | K | N/A | Aston and Szasz, 1947 | Uncertainty assigned by TRC = 0.05 K; TRC |
Ttriple | 136.94 | K | N/A | Tooke and Aston, 1945 | Uncertainty assigned by TRC = 0.08 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 23.68 | kJ/mol | N/A | Majer and Svoboda, 1985 | |
ΔvapH° | 23.9 | kJ/mol | N/A | Reid, 1972 | AC |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
24.623 | 273.24 | N/A | Aston and Szasz, 1947, 2 | P = 66.41 kPa; DH |
24.02 | 284. | N/A | Majer and Svoboda, 1985 | |
25.3 | 276. | A | Stephenson and Malanowski, 1987 | Based on data from 243. to 291. K.; AC |
26.4 | 228. | A | Stephenson and Malanowski, 1987 | Based on data from 204. to 243. K.; AC |
24.6 ± 0.3 | 273.25 | C | Aston and Szasz, 1947, 3 | ALS |
24.6 ± 0.1 | 273. | C | Aston and Szasz, 1947, 2 | AC |
25.2 | 276. | N/A | Stull, 1947 | Based on data from 184. to 291. K.; AC |
Entropy of vaporization
ΔvapS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
90.11 | 273.24 | Aston and Szasz, 1947, 2 | P; DH |
Antoine Equation Parameters
log10(P) = A − (B / (T + C))
P = vapor pressure (bar)
T = temperature (K)
View plot Requires a JavaScript / HTML 5 canvas capable browser.
Temperature (K) | A | B | C | Reference | Comment |
---|---|---|---|---|---|
184. to 291.7 | 3.78159 | 941.601 | -42.565 | Stull, 1947 | Coefficents calculated by NIST from author's data. |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
6.9613 | 136.92 | Aston and Szasz, 1947, 2 | DH |
6.95 | 136.9 | Domalski and Hearing, 1996 | AC |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
50.84 | 136.92 | Aston and Szasz, 1947, 2 | DH |
References
Go To: Top, Gas phase thermochemistry data, Phase change data, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Prosen, Maron, et al., 1951
Prosen, E.J.; Maron, F.W.; Rossini, F.D.,
Heats of combustion, formation, and insomerization of ten C4 hydrocarbons,
J. Res. NBS, 1951, 46, 106-112. [all data]
Prosen, Maron, et al., 1949
Prosen, E.J.; Maron, F.W.; Rossini, F.D.,
Heat of isomerization of the two butadienes,
J. Res. NBS, 1949, 42, 269-275. [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]
Kilpatrick J.E., 1949
Kilpatrick J.E.,
Heats, equilibrium constants, and free energies of formation of the C3 to C5 diolefins, styrene, and the methylstyrenes,
J. Res. Nat. Bur. Stand., 1949, 42, 225-240. [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]
Feugeas and Giusti, 1968
Feugeas, C.; Giusti, G.L.,
C. R. Acad. Sci. Paris, Ser. C, 1968, 267, 84. [all data]
Streiff, Murphy, et al., 1946
Streiff, A.J.; Murphy, E.T.; Cahill, J.C.; Soule, L.F.; Sedlak, V.A.; Willingham, C.B.; Rossini, F.D.,
, Am. Pet. Inst. Res. Proj. 6, unpublished, Natl. Bur. Stand., 1946. [all data]
Hurd and Meinert, 1931
Hurd, C.D.; Meinert, R.N.,
Synthesis and pyrolysis of methylallene and ethylacetylene,
J. Am. Chem. Soc., 1931, 53, 289-300. [all data]
Streiff, Murphy, et al., 1947
Streiff, A.J.; Murphy, E.T.; Zimmerman, J.C.; Soule, L.F.; Sedlak, V.A.; Willingham, C.B.; Rossini, F.D.,
Purification, purity, and freezing points of n-decane, 4 alkylcyclopentanes 9 alkylcyclohexanes, 2 monoolefins, 1,2-butadiene, and 2-butyne of the API-standard and API-NBS series.,
J. Res. Natl. Bur. Stand. (U. S.), 1947, 39, 321. [all data]
Aston and Szasz, 1947
Aston, J.G.; Szasz, G.J.,
The Thermodynamics of Butadiene-1,2 from Calorimetric and Spectroscopic Data,
J. Am. Chem. Soc., 1947, 69, 3108. [all data]
Tooke and Aston, 1945
Tooke, J.W.; Aston, J.G.,
Solid Solutions in Hydrocarbon Systems,
J. Am. Chem. Soc., 1945, 67, 2275. [all data]
Reid, 1972
Reid, Robert C.,
Handbook on vapor pressure and heats of vaporization of hydrocarbons and related compounds, R. C. Wilhort and B. J. Zwolinski, Texas A Research Foundation. College Station, Texas(1971). 329 pages.$10.00,
AIChE J., 1972, 18, 6, 1278-1278, https://doi.org/10.1002/aic.690180637
. [all data]
Aston and Szasz, 1947, 2
Aston, J.G.; Szasz, G.J.,
The thermodynamics of butadiene-1,2 from calorimetric and spectroscopic data,
J. Am. Chem. Soc., 1947, 69, 3108-3114. [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]
Aston and Szasz, 1947, 3
Aston, J.G.; Szasz, G.J.,
The thermodynamics of butadiene-1,2 from calorimetric and spectroscopic data,
J. Am. Chem. Soc., 1947, 69, 3108-31. [all data]
Stull, 1947
Stull, Daniel R.,
Vapor Pressure of Pure Substances. Organic and Inorganic Compounds,
Ind. Eng. Chem., 1947, 39, 4, 517-540, https://doi.org/10.1021/ie50448a022
. [all data]
Domalski and Hearing, 1996
Domalski, Eugene S.; Hearing, Elizabeth D.,
Heat Capacities and Entropies of Organic Compounds in the Condensed Phase. Volume III,
J. Phys. Chem. Ref. Data, 1996, 25, 1, 1, https://doi.org/10.1063/1.555985
. [all data]
Notes
Go To: Top, Gas phase thermochemistry data, Phase change data, References
- Symbols used in this document:
Cp,gas Constant pressure heat capacity of gas Tboil Boiling point Tfus Fusion (melting) point Ttriple Triple point temperature ΔcH°gas Enthalpy of combustion of gas at standard conditions ΔfH°gas Enthalpy of formation of gas at standard conditions ΔfusH Enthalpy of fusion ΔfusS Entropy of fusion ΔvapH Enthalpy of vaporization ΔvapH° Enthalpy of vaporization at standard conditions ΔvapS Entropy of vaporization - 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.