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, 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
Go To: Top, Gas phase thermochemistry data, Phase change data, Reaction 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 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
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Reaction 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
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, 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
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction 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 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 |
References
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry 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.
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,
J. Am. Chem. Soc., 1936, 58, 134-137. [all data]
Takeda, Yamamuro, et al., 1991, 2
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, 52, 607. [all data]
Chao, Hall, et al., 1983, 2
Chao, J.; Hall, K.R.; Yao, J.M.,
Thermodynamic Properties of Simple Alkenes,
Thermochim. Acta, 1983, 64, 285. [all data]
Aston, Finke, et al., 1946
Aston, J.G.; Finke, 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. [all data]
Tsonopoulos and Ambrose, 1996
Tsonopoulos, C.; Ambrose, D.,
Vapor-Liquid Critical Properties of Elements and Compounds. 6. Unsaturated Aliphatic Hydrocarbons,
J. Chem. Eng. Data, 1996, 41, 645-656. [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]
Coffin and Maass, 1928
Coffin, C.C.; Maass, O.,
The Preparation and Physical Properties of α-,β- and γ-Butylene and Normal and Isobutane,
J. Am. Chem. Soc., 1928, 50, 1427-37. [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]
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]
Lamb and Roper, 1940
Lamb, Arthur B.; Roper, Edwin E.,
The Vapor Pressures of Certain Unsaturated Hydrocarbons,
J. Am. Chem. Soc., 1940, 62, 4, 806-814, https://doi.org/10.1021/ja01861a032
. [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]
Coffin and Maass, 1928, 2
Coffin, C.C.; Maass, O.,
The Preparation and Physical Properties of α, β- and γ-Butylene and Normal and Isobutane,
J. Am. Chem. Soc., 1928, 50, 5, 1427-1437, https://doi.org/10.1021/ja01392a028
. [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]
Meyer and Stroz, 1972
Meyer, E.F.; Stroz, D.G.,
Thermodynamics of n-butene isomerization,
J. Am. Chem. Soc., 1972, 94, 6344-6347. [all data]
Cox and Pilcher, 1970
Cox, J.D.; Pilcher, G.,
Thermochemistry of Organic and Organometallic Compounds, Academic Press, New York, 1970, 1-636. [all data]
Happel, Hnatow, et al., 1971
Happel, J.; Hnatow, M.A.; Mezaki, R.,
Isomerization equilibrium constants of n-butenes,
J. Chem. Eng. Data, 1971, 16, 206-209. [all data]
Maccoll and Ross, 1965
Maccoll, A.; Ross, R.A.,
The hydrogen bromide catalyzed isomerization of n-butenes. I. equilibrium values,
J. Am. Chem. Soc., 1965, 87, 1169-1170. [all data]
Golden, Egger, et al., 1964
Golden, D.M.; Egger, K.W.; Benson, S.W.,
Iodine-catalyzed isomerization of olefins. I. Thermodynamics data from equilibrium studies of positional and geometrical isomerization of 1-butene and 2-butene,
J. Am. Chem. Soc., 1964, 86, 5416-5420. [all data]
Levanova and Andreevskii, 1964
Levanova, S.V.; Andreevskii, D.N.,
The equilibrium of 2-chlorobutane dehydrochlorination,
Neftekhimiya, 1964, 4, 329-336. [all data]
DePuy, Gronert, et al., 1989
DePuy, C.H.; Gronert, S.; Barlow, S.E.; Bierbaum, V.M.; Damrauer, R.,
The Gas Phase Acidities of the Alkanes,
J. Am. Chem. Soc., 1989, 111, 6, 1968, https://doi.org/10.1021/ja00188a003
. [all data]
Peerboom, Rademaker, et al., 1992
Peerboom, R.A.L.; Rademaker, G.J.; Dekoning, L.J.; Nibbering, N.M.M.,
Stabilization of Cycloalkyl Carbanions in the Gas Phase,
Rapid Commun. Mass Spectrom., 1992, 6, 6, 394, https://doi.org/10.1002/rcm.1290060608
. [all data]
Lister, 1941
Lister, M.W.,
Heats of organic reactions. X. Heats of bromination of cyclic olefins,
J. Am. Chem. Soc., 1941, 63, 143-149. [all data]
Conn, Kistiakowsky, et al., 1938
Conn, J.B.; Kistiakowsky, G.B.; Smith, E.A.,
Heats of organic reactions. VII. Addition of halogens to olefins,
J. Am. Chem. Soc., 1938, 60, 2764-2771. [all data]
Lacher, Billings, et al., 1952
Lacher, J.R.; Billings, T.J.; Campion, D.E.,
Vapor phase heats of hydrobromination of the isomeric butenes,
J. Am. Chem. Soc., 1952, 74, 5291-52. [all data]
Graul and Squires, 1990
Graul, S.T.; Squires, R.R.,
Gas-Phase Acidities Derived from Threshold Energies for Activated Reactions,
J. Am. Chem. Soc., 1990, 112, 7, 2517, https://doi.org/10.1021/ja00163a007
. [all data]
Cline and Kistiakowsky, 1937
Cline, J.E.; Kistiakowsky, G.B.,
The gaseous equilibrium of 1,2-diiodobutane, butene-1 and iodine,
J. Chem. Phys., 1937, 5, 990. [all data]
Kistiakowsky, Ruhoff, et al., 1935
Kistiakowsky, G.B.; Ruhoff, J.R.; Smith, H.A.; Vaughan, W.E.,
Heats of organic reactions. II. Hydrogenation of some simpler olefinic hydrocarbons,
J. Am. Chem. Soc., 1935, 57, 876-882. [all data]
Kukui, Potolovskii, et al., 1973
Kukui, N.M.; Potolovskii, L.A.; Vasileva, V.N.,
Thermochemical and thermodynamic calculation of the alkylation of phenol by normal α-olefins,
Khim. Tekhnol. Topl. Masel, 1973, 18, 10-13. [all data]
Notes
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- Symbols used in this document:
Cp,gas Constant pressure heat capacity of gas Cp,liquid Constant pressure heat capacity of liquid 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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