1-Butene
- Formula: C4H8
- Molecular weight: 56.1063
- IUPAC Standard InChIKey: VXNZUUAINFGPBY-UHFFFAOYSA-N
- CAS Registry Number: 106-98-9
- 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: α-Butene; α-Butylene; But-1-ene; Butene-1; Ethylethylene; 1-Butylene; 1-C4H8
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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), 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 | -0.63 ± 0.79 | kJ/mol | Cm | Prosen, Maron, et al., 1951 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°gas | -2716.8 ± 0.75 | kJ/mol | Cm | Prosen, Maron, et al., 1951 | Corresponding ΔfHºgas = -0.54 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 |
---|---|---|---|
41.05 | 50. | Thermodynamics Research Center, 1997 | p=1 bar. Calculated values of the thermodynamic functions [ Aston J.D., 1946, Kilpatrick J.E., 1946, Durig J.R., 1980, Thermodynamics Research Center, 1997] show some disagreement between authors as well as with experimental data [ Aston J.D., 1946, 2, Wacker P.F., 1947] (up to 3-4 J/mol*K). More reliable experimental data are required to solve available inconsistency.; GT |
48.05 | 100. | ||
56.41 | 150. | ||
65.19 | 200. | ||
80.03 | 273.15 | ||
85.56 | 298.15 | ||
85.98 | 300. | ||
108.48 | 400. | ||
129.06 | 500. | ||
146.75 | 600. | ||
161.88 | 700. | ||
174.91 | 800. | ||
186.21 | 900. | ||
196.02 | 1000. | ||
204.55 | 1100. | ||
211.96 | 1200. | ||
218.41 | 1300. | ||
224.02 | 1400. | ||
228.91 | 1500. | ||
238.64 | 1750. | ||
245.70 | 2000. | ||
250.92 | 2250. | ||
254.85 | 2500. | ||
257.85 | 2750. | ||
260.16 | 3000. |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
89.58 ± 0.06 | 313.55 | Wacker P.F., 1947 | GT |
101.21 ± 0.07 | 363.25 |
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 by: Eugene S. Domalski and Elizabeth D. Hearing
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
S°liquid | 229.06 | J/mol*K | N/A | Takeda, Yamamuro, et al., 1991 | |
S°liquid | 227.0 | J/mol*K | N/A | Chao, Hall, et al., 1983 | |
S°liquid | 213.84 | J/mol*K | N/A | Aston, Fink, et al., 1946 |
Constant pressure heat capacity of liquid
Cp,liquid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
128.96 | 298.15 | Takeda, Yamamuro, et al., 1991 | T = 5 to 300 K. |
118. | 298.15 | Chao, Hall, et al., 1983 | T = 12 to 360 K. |
128.6 | 294. | Schlinger and Sage, 1949 | T = 294 to 378 K. Cp given as 0.548 Btu/lb*R at 70°F at bubble point. |
119.45 | 260. | Aston, Fink, et al., 1946 | T = 11.5 to 260 K. |
119.16 | 253.4 | Todd and Parks, 1936 | T = 81 to 253 K. Value is unsmoothed experimental datum. |
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
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 | 266.8 ± 0.5 | K | AVG | N/A | Average of 15 out of 17 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 87.800 | K | N/A | Takeda, Yamamuro, et al., 1991, 2 | Uncertainty assigned by TRC = 0.005 K; TRC |
Ttriple | 87.82 | K | N/A | Chao, Hall, et al., 1983, 2 | Uncertainty assigned by TRC = 0.02 K; TRC |
Ttriple | 87.8 | K | N/A | Aston, Finke, et al., 1946 | Uncertainty assigned by TRC = 0.05 K; TRC |
Ttriple | 87.83 | K | N/A | Aston, Finke, et al., 1946 | Uncertainty assigned by TRC = 0.05 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 419.5 ± 0.5 | K | N/A | Tsonopoulos and Ambrose, 1996 | |
Tc | 419.6 | K | N/A | Majer and Svoboda, 1985 | |
Tc | 417.15 | K | N/A | Coffin and Maass, 1928 | Uncertainty assigned by TRC = 2. K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 40.2 ± 0.5 | bar | N/A | Tsonopoulos and Ambrose, 1996 | |
Quantity | Value | Units | Method | Reference | Comment |
Vc | 0.2408 | l/mol | N/A | Tsonopoulos and Ambrose, 1996 | |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 4.15 ± 0.05 | mol/l | N/A | Tsonopoulos and Ambrose, 1996 | |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 20.88 | kJ/mol | N/A | Majer and Svoboda, 1985 | |
ΔvapH° | 20.1 | kJ/mol | N/A | Reid, 1972 | AC |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
21.866 | 266.91 | N/A | Aston, Fink, et al., 1946 | P = 101.325 kPa; DH |
22.07 | 266.9 | N/A | Majer and Svoboda, 1985 | |
23.3 | 259. | A | Stephenson and Malanowski, 1987 | Based on data from 200. to 274. K.; AC |
28.3 | 177. | A | Stephenson and Malanowski, 1987 | Based on data from 126. to 192. K.; AC |
22.8 | 282. | A | Stephenson and Malanowski, 1987 | Based on data from 267. to 345. K.; AC |
22.0 | 357. | A | Stephenson and Malanowski, 1987 | Based on data from 342. to 411. K.; AC |
22.5 | 282. | A | Stephenson and Malanowski, 1987 | Based on data from 267. to 411. K.; AC |
23.701 | 202. | C | Aston, Fink, et al., 1946 | ALS |
25.3 | 202. | N/A | Aston, Fink, et al., 1946 | AC |
24.5 | 219. | N/A | Aston, Fink, et al., 1946 | AC |
23.3 | 242. | N/A | Aston, Fink, et al., 1946 | AC |
21.9 | 267. | N/A | Aston, Fink, et al., 1946 | AC |
23.2 | 258. | N/A | Lamb and Roper, 1940 | Based on data from 216. to 273. K. See also Boublik, Fried, et al., 1984.; AC |
Enthalpy of vaporization
ΔvapH = A exp(-αTr)
(1 − Tr)β
ΔvapH =
Enthalpy of vaporization (at saturation pressure)
(kJ/mol)
Tr = reduced temperature (T / Tc)
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Temperature (K) | 203. to 378. |
---|---|
A (kJ/mol) | 32.51 |
α | 0.0052 |
β | 0.38 |
Tc (K) | 419.6 |
Reference | Majer and Svoboda, 1985 |
Entropy of vaporization
ΔvapS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
81.92 | 266.91 | Aston, Fink, et al., 1946 | P; DH |
Antoine Equation Parameters
log10(P) = A − (B / (T + C))
P = vapor pressure (bar)
T = temperature (K)
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Temperature (K) | A | B | C | Reference | Comment |
---|---|---|---|---|---|
195.7 to 269.4 | 4.24696 | 1099.207 | -8.256 | Coffin and Maass, 1928, 2 | Coefficents calculated by NIST from author's data. |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
3.9586 | 87.81 | Takeda, Yamamuro, et al., 1991 | DH |
3.848 | 87.82 | Chao, Hall, et al., 1983 | DH |
3.849 | 87.82 | Aston, Fink, et al., 1946 | DH |
3.85 | 87.8 | Domalski and Hearing, 1996 | AC |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
45.09 | 87.81 | Takeda, Yamamuro, et al., 1991 | DH |
43.8 | 87.82 | Chao, Hall, et al., 1983 | DH |
43.83 | 87.82 | Aston, Fink, et al., 1946 | DH |
Reaction thermochemistry data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics data, IR Spectrum, Mass spectrum (electron ionization), 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
B - John E. Bartmess
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
By formula: C4H8 = C4H8
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -12.6 ± 0.84 | kJ/mol | Eqk | Meyer and Stroz, 1972 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -11.0 kJ/mol; At 300 K; ALS |
ΔrH° | -12.4 ± 1.7 | kJ/mol | Eqk | Happel, Hnatow, et al., 1971 | gas phase; ALS |
ΔrH° | -12.7 | kJ/mol | Eqk | Maccoll and Ross, 1965 | gas phase; GC; ALS |
ΔrH° | -11.7 ± 0.84 | kJ/mol | Eqk | Golden, Egger, et al., 1964 | gas phase; ALS |
ΔrH° | -11.5 | kJ/mol | Ciso | Levanova and Andreevskii, 1964 | gas phase; At 420.3 K; ALS |
C4H7- + =
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1724. ± 8.4 | kJ/mol | Bran | DePuy, Gronert, et al., 1989 | gas phase; B |
ΔrH° | 1729. ± 20. | kJ/mol | Bran | Peerboom, Rademaker, et al., 1992 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1690. ± 8.8 | kJ/mol | H-TS | DePuy, Gronert, et al., 1989 | gas phase; B |
ΔrG° | 1695. ± 21. | kJ/mol | H-TS | Peerboom, Rademaker, et al., 1992 | gas phase; B |
By formula: C4H8 + Br2 = C4H8Br2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -120.9 | kJ/mol | Cm | Lister, 1941 | gas phase; Heat of bromination at 300 K; ALS |
ΔrH° | -123.2 ± 0.84 | kJ/mol | Cm | Conn, Kistiakowsky, et al., 1938 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -123.8 ± 0.84 kJ/mol; At 355 °K; ALS |
By formula: HBr + C4H8 = C4H9Br
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -83.85 ± 0.50 | kJ/mol | Cm | Lacher, Billings, et al., 1952 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -84.3 ± 7.5 kJ/mol; Heat of hydrobromination at 367 K; ALS |
C4H7- + =
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1707. ± 15. | kJ/mol | CIDT | Graul and Squires, 1990 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1674. ± 15. | kJ/mol | H-TS | Graul and Squires, 1990 | gas phase; B |
By formula: C4H8 = C4H8
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -10.6 ± 2.1 | kJ/mol | Eqk | Happel, Hnatow, et al., 1971 | gas phase; ALS |
ΔrH° | -8.16 | kJ/mol | Ciso | Levanova and Andreevskii, 1964 | gas phase; At 420.3 K; ALS |
By formula: C4H8I2 = C4H8 + I2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 50.2 ± 6.3 | kJ/mol | Cm | Cline and Kistiakowsky, 1937 | gas phase; Heat of formation derived by Cox and Pilcher, 1970; ALS |
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -125.9 ± 0.42 | kJ/mol | Chyd | Kistiakowsky, Ruhoff, et al., 1935 | gas phase; At 355 °K; ALS |
By formula: C4H9Cl = C4H8 + HCl
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 75.31 | kJ/mol | Eqk | Levanova and Andreevskii, 1964 | gas phase; At 420 K; ALS |
By formula: C4H8 + I2 = C4H8I2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -50.2 ± 6.3 | kJ/mol | Cm | Cline and Kistiakowsky, 1937 | gas phase; ALS |
By formula: C10H14O = C4H8 + C6H6O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 77.8 | kJ/mol | Cm | Kukui, Potolovskii, et al., 1973 | liquid phase; ALS |
By formula: C10H14O = C4H8 + C6H6O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 82.8 | kJ/mol | Cm | Kukui, Potolovskii, et al., 1973 | 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 |
---|---|---|---|---|
0.0040 | Q | N/A | missing citation give several references for the Henry's law constants but don't assign them to specific species. | |
0.0014 | L | N/A | ||
0.013 | 6400. | L | N/A | |
0.0040 | V | 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), 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:
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 C4H8+ (ion structure unspecified)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
IE (evaluated) | 9.55 ± 0.06 | eV | N/A | N/A | L |
Ionization energy determinations
IE (eV) | Method | Reference | Comment |
---|---|---|---|
9.55 ± 0.06 | PIPECO | Van der Meij, Van Eck, et al., 1989 | LL |
9.57 | PI | Traeger, 1986 | LBLHLM |
9.58 | PI | Traeger, 1984 | LBLHLM |
9.62 ± 0.05 | EI | Holmes and Lossing, 1983 | LBLHLM |
9.59 ± 0.02 | PI | Wood and Taylor, 1979 | LLK |
9.63 ± 0.02 | PE | Bieri, Burger, et al., 1977 | LLK |
9.625 ± 0.003 | PE | Masclet, Grosjean, et al., 1973 | LLK |
9.58 | EI | Lossing, 1972 | LLK |
9.59 | PE | Dewar and Worley, 1969 | RDSH |
9.62 | CI | Cermak, 1968 | RDSH |
9.61 ± 0.02 | PI | Steiner, Giese, et al., 1961 | RDSH |
9.58 ± 0.01 | PI | Watanabe, 1957 | RDSH |
9.77 ± 0.01 | PE | Krause, Taylor, et al., 1978 | Vertical value; LLK |
10.0 | PE | White, Carlson, et al., 1974 | Vertical value; LLK |
9.72 | PE | Mollere, Bock, et al., 1972 | Vertical value; LLK |
Appearance energy determinations
Ion | AE (eV) | Other Products | Method | Reference | Comment |
---|---|---|---|---|---|
CH3+ | 14.1 | C3H5 | EI | SenSharma and Franklin, 1973 | LLK |
C2H3+ | 13.6 | ? | EI | Omura, 1962 | RDSH |
C2H4+ | 11.65 ± 0.06 | C2H4 | PIPECO | Van der Meij, Van Eck, et al., 1989 | LL |
C2H4+ | 11.7 ± 0.2 | ? | EI | Meisels, Park, et al., 1970 | RDSH |
C2H5+ | 14.22 ± 0.06 | C2H3 | PIPECO | Van der Meij, Van Eck, et al., 1989 | LL |
C3H3+ | 14.07 ± 0.10 | H2+CH3 | PIPECO | Van der Meij, Van Eck, et al., 1989 | LL |
C3H3+ | 13.82 | ? | EI | Omura, 1961 | RDSH |
C3H5+ | 11.36 ± 0.06 | CH3 | PIPECO | Van der Meij, Van Eck, et al., 1989 | LL |
C3H5+ | 11.20 | CH3 | PI | Traeger, 1984 | LBLHLM |
C3H5+ | 11.8 | CH3 | EI | SenSharma and Franklin, 1973 | LLK |
C3H5+ | 11.28 | CH3 | EI | Lossing, 1971 | LLK |
C4H5+ | 14.33 ± 0.07 | H2+H | PIPECO | Van der Meij, Van Eck, et al., 1989 | LL |
C4H7+ | 11.17 ± 0.06 | H | PIPECO | Van der Meij, Van Eck, et al., 1989 | LL |
C4H7+ | 11.13 | H | PI | Traeger, 1986 | LBLHLM |
C4H7+ | 11.26 | H | EI | Lossing, 1972 | LLK |
De-protonation reactions
C4H7- + =
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1724. ± 8.4 | kJ/mol | Bran | DePuy, Gronert, et al., 1989 | gas phase; B |
ΔrH° | 1729. ± 20. | kJ/mol | Bran | Peerboom, Rademaker, et al., 1992 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1690. ± 8.8 | kJ/mol | H-TS | DePuy, Gronert, et al., 1989 | gas phase; B |
ΔrG° | 1695. ± 21. | kJ/mol | H-TS | Peerboom, Rademaker, et al., 1992 | gas phase; B |
C4H7- + =
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1707. ± 15. | kJ/mol | CIDT | Graul and Squires, 1990 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1674. ± 15. | kJ/mol | H-TS | Graul and Squires, 1990 | gas phase; B |
IR Spectrum
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, Mass spectrum (electron ionization), 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: NIST Mass Spectrometry Data Center, William E. Wallace, director
Gas Phase Spectrum
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Additional Data
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Download spectrum in JCAMP-DX format.
Owner | NIST Standard Reference Data Program Collection (C) 2018 copyright by the U.S. Secretary of Commerce on behalf of the United States of America. All rights reserved. |
---|---|
Origin | Sadtler Research Labs Under US-EPA Contract |
State | gas |
Mass spectrum (electron ionization)
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, 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: NIST Mass Spectrometry Data Center, William E. Wallace, director
Spectrum
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Additional Data
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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. |
---|---|
NIST MS number | 18918 |
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), 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]
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]
Aston J.D., 1946
Aston J.D.,
Thermodynamic properties of gaseous 1,3-butadiene and normal butenes above 25 C. Equilibria in the system 1,3-butadiene, n-butenes, and n-butane,
J. Chem. Phys., 1946, 14, 67-79. [all data]
Kilpatrick J.E., 1946
Kilpatrick J.E.,
Heat content, free energy function, entropy, and heat capacity of ethylene, propylene, and the four butenes to 1500 K,
J. Res. Nat. Bur. Stand, 1946, 37, 163-171. [all data]
Durig J.R., 1980
Durig J.R.,
Spectroscopic and thermodynamic study of conformational properties and torsional potential functions of 1-butene,
J. Phys. Chem., 1980, 84, 773-781. [all data]
Aston J.D., 1946, 2
Aston J.D.,
The heat capacity and entropy, heats of fusion and vaporization and the vapor pressure of butene-1. The zero point entropy of the glass. The entropy of the gas from molecular data,
J. Am. Chem. Soc., 1946, 68, 52-57. [all data]
Wacker P.F., 1947
Wacker P.F.,
Heat capacities of gaseous oxygen, isobutane, and 1-butene from -30 to +90 C,
J. Res. Nat. Bur. Stand., 1947, 38, 651-659. [all data]
Takeda, Yamamuro, et al., 1991
Takeda, K.; Yamamuro, O.; Suga, H.,
Thermodynamic study of 1-butene. Exothermic and endothermic enthalpy relaxations near the glass transition,
J. Phys. Chem. Solids, 1991, 22, 607-615. [all data]
Chao, Hall, et al., 1983
Chao, J.; Hall, K.R.; Yao, J.M.,
Thermodynamic properties of simple alkenes,
Thermochim. Acta, 1983, 64(3), 285-303. [all data]
Aston, Fink, et al., 1946
Aston, J.G.; Fink, H.L.; Bestul, A.B.; Pace, E.L.; Szasz, G.J.,
The heat capacity and entropy, heats of fusion and vaporization and the vapor pressure of butene-1. The zero point entropy of the glass. The entropy of the gas from molecular data,
J. Am. Chem. Soc., 1946, 68, 52-57. [all data]
Schlinger and Sage, 1949
Schlinger, W.G.; Sage, B.H.,
Isobaric heat capacity of 1-butene and 1-pentene at bubble point,
Ind. Eng. Chem., 1949, 41, 1779-1782. [all data]
Todd and Parks, 1936
Todd, S.S.; Parks, G.S.,
Thermal data on organic compounds. XV. Some heat capacity, entropy and free energy data for the isomeric butenes,
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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 S°liquid Entropy of liquid at standard conditions Tboil Boiling point Tc Critical temperature Ttriple Triple point temperature Vc Critical volume d(ln(kH))/d(1/T) Temperature dependence parameter for Henry's Law constant k°H Henry's Law constant at 298.15K 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 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 ΔvapS Entropy of vaporization ρc Critical density - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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