2-Butene, (Z)-
- Formula: C4H8
- Molecular weight: 56.1063
- IUPAC Standard InChIKey: IAQRGUVFOMOMEM-ARJAWSKDSA-N
- CAS Registry Number: 590-18-1
- 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. - Stereoisomers:
- Other names: (Z)-2-Butene; cis-Butene; cis-2-Butylene; cis-1,2-Dimethylethylene; cis-2-Butene; (Z)-2-C4H8; (2Z)-2-Butene; 2-Butene, cis-; Butene-2, cis-; 2-Butene, (2Z)-; (Z)-but-2-ene
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Gas phase thermochemistry data
Go To: Top, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Gas Chromatography, 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 | -7.7 ± 1.3 | kJ/mol | Cm | Prosen, Maron, et al., 1951 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°gas | -2709.8 ± 1.2 | kJ/mol | Cm | Prosen, Maron, et al., 1951 | Corresponding ΔfHºgas = -7.57 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 |
---|---|---|---|
45.01 | 50. | Thermodynamics Research Center, 1997 | p=1 bar. The difference between recommended values and obtained by [ Aston J.D., 1946] is inside the range of uncertainties of these two statistical calculations. The values of S and Cp calculated by [ Scott R.B., 1944] and [ Kilpatrick J.E., 1946] are little lower than recommended ones.; GT |
51.23 | 100. | ||
55.45 | 150. | ||
61.73 | 200. | ||
74.89 | 273.15 | ||
80.15 | 298.15 | ||
80.55 | 300. | ||
102.73 | 400. | ||
123.64 | 500. | ||
141.91 | 600. | ||
157.66 | 700. | ||
171.27 | 800. | ||
183.06 | 900. | ||
193.30 | 1000. | ||
202.18 | 1100. | ||
209.90 | 1200. | ||
216.59 | 1300. | ||
222.41 | 1400. | ||
227.48 | 1500. | ||
237.55 | 1750. | ||
244.85 | 2000. | ||
250.26 | 2250. | ||
254.33 | 2500. | ||
257.45 | 2750. | ||
259.87 | 3000. |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
70.8 ± 1.6 | 250. | Scott R.B., 1944 | Please also see Kistiakowsky G.B., 1940.; GT |
71.1 ± 1.6 | 255. | ||
71.7 ± 1.7 | 260. | ||
72.3 ± 1.7 | 265. | ||
72.9 ± 1.7 | 270. | ||
73.9 ± 1.7 | 275. | ||
74.7 ± 1.7 | 280. | ||
75.9 ± 1.8 | 285. | ||
77.2 ± 1.8 | 290. | ||
78.5 ± 1.8 | 295. | ||
81.13 ± 0.16 | 298.58 | ||
79.9 ± 1.8 | 300. | ||
88.24 ± 0.18 | 332.85 | ||
96.27 ± 0.19 | 371.24 |
Condensed phase thermochemistry data
Go To: Top, Gas phase thermochemistry data, Phase change data, Reaction thermochemistry data, Gas Chromatography, 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 | 220. | J/mol*K | N/A | Chao, Hall, et al., 1983 | |
S°liquid | 219.91 | J/mol*K | N/A | Scott, Ferguson, et al., 1944 | |
S°liquid | 212.88 | J/mol*K | N/A | Todd and Parks, 1936 | Extrapolation below 90 K, 48.95 J/mol*K. |
Constant pressure heat capacity of liquid
Cp,liquid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
127. | 298.15 | Chao, Hall, et al., 1983 | T = 5 to 367 K. |
130.00 | 299.8 | Schlinger and Sage, 1952 | T = 80 to 200°F. |
126.15 | 298.15 | Scott, Ferguson, et al., 1944 | T = 15 to 300 K. |
118.87 | 266.6 | Todd and Parks, 1936 | T = 93 to 267 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
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
DH - Eugene S. Domalski and Elizabeth D. Hearing
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 276.84 ± 0.08 | K | AVG | N/A | Average of 7 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 133.85 | K | N/A | Kistiakowsky, Ruhoff, et al., 1935 | Uncertainty assigned by TRC = 0.5 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 134.26 | K | N/A | Chao, Hall, et al., 1983, 2 | Uncertainty assigned by TRC = 0.02 K; TRC |
Ttriple | 134.26 | K | N/A | Scott, Ferguson, et al., 1944 | Uncertainty assigned by TRC = 0.02 K; TRC |
Ttriple | 133.8 | K | N/A | Todd and Parks, 1936, 2 | Uncertainty assigned by TRC = 0.2 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 435.5 ± 0.1 | K | N/A | Tsonopoulos and Ambrose, 1996 | |
Tc | 435.6 | K | N/A | Majer and Svoboda, 1985 | |
Tc | 435.55 | K | N/A | Ambrose, Cox, et al., 1960 | Uncertainty assigned by TRC = 0.3 K; Visual, PRT, IPTS-48; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 42.1 ± 0.5 | bar | N/A | Tsonopoulos and Ambrose, 1996 | |
Quantity | Value | Units | Method | Reference | Comment |
Vc | 0.2338 | l/mol | N/A | Tsonopoulos and Ambrose, 1996 | |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 4.28 ± 0.05 | mol/l | N/A | Tsonopoulos and Ambrose, 1996 | |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 22.7 | kJ/mol | N/A | Majer and Svoboda, 1985 | |
ΔvapH° | 22.1 | kJ/mol | N/A | Reid, 1972 | AC |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
23.34 | 276.9 | N/A | Majer and Svoboda, 1985 | |
24.4 | 275. | A | Stephenson and Malanowski, 1987 | Based on data from 221. to 290. K.; AC |
24.0 | 291. | A | Stephenson and Malanowski, 1987 | Based on data from 276. to 325. K.; AC |
23.6 | 339. | A | Stephenson and Malanowski, 1987 | Based on data from 324. to 386. K.; AC |
23.6 | 398. | A | Stephenson and Malanowski, 1987 | Based on data from 383. to 431. K.; AC |
22.5 | 246. | C | Scott, Ferguson, et al., 1944, 2 | AC |
22.47 | 246. | C | Scott, Ferguson, et al., 1944 | ALS |
24.31 | 276.73 | V | Kistiakowsky, Ruhoff, et al., 1935, 2 | At 355 °K; ALS |
25.3 | 252. | N/A | Hopkins, 1921 | Based on data from 195. to 267. K. See also Boublik, Fried, et al., 1984.; AC |
Enthalpy of vaporization
ΔvapH =
A exp(-βTr) (1 − Tr)β
ΔvapH =
Enthalpy of vaporization (at saturation pressure)
(kJ/mol)
Tr = reduced temperature (T / Tc)
View plot Requires a JavaScript / HTML 5 canvas capable browser.
Temperature (K) | A (kJ/mol) | β | Tc (K) | Reference | Comment |
---|---|---|---|---|---|
246. to 292. | 36.37 | 0.2696 | 435.6 | Majer and Svoboda, 1985 |
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 |
---|---|---|---|---|---|
203.06 to 295.91 | 3.98744 | 957.06 | -36.504 | Scott, Ferguson, et al., 1944 | Coefficents calculated by NIST from author's data. |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
7.309 | 134.26 | Chao, Hall, et al., 1983 | DH |
7.3092 | 134.26 | Scott, Ferguson, et al., 1944 | DH |
7.31 | 134.3 | Domalski and Hearing, 1996 | AC |
7.318 | 133.8 | Todd and Parks, 1936 | DH |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
54.4 | 134.26 | Chao, Hall, et al., 1983 | DH |
54.44 | 134.26 | Scott, Ferguson, et al., 1944 | DH |
54.69 | 133.8 | Todd and Parks, 1936 | DH |
Reaction thermochemistry data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Gas Chromatography, 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
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° | -4. ± 2. | kJ/mol | AVG | N/A | Average of 7 values; Individual data points |
By formula: HBr + C4H8 = C4H9Br
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -77.07 ± 0.50 | kJ/mol | Cm | Lacher, Billings, et al., 1952 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -76.8 ± 6.6 kJ/mol; Heat of Hydrobromination at 373 K |
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -118.5 ± 0.42 | kJ/mol | Chyd | Kistiakowsky, Ruhoff, et al., 1935, 2 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -119.54 ± 0.079 kJ/mol; At 355 °K |
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 |
ΔrH° | -8.16 | kJ/mol | Ciso | Levanova and Andreevskii, 1964 | gas phase; At 420.3 K |
By formula: C4H8 + Br2 = C4H8Br2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -126.3 ± 0.84 | kJ/mol | Cm | Conn, Kistiakowsky, et al., 1938 | gas phase; At 355 °K |
By formula: C4H9Cl = C4H8 + HCl
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 67.15 | kJ/mol | Eqk | Levanova and Andreevskii, 1964 | gas phase; At 420 K |
Gas Chromatography
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: NIST Mass Spectrometry Data Center, William E. Wallace, director
Kovats' RI, non-polar column, isothermal
Column type | Active phase | Temperature (C) | I | Reference | Comment |
---|---|---|---|---|---|
Capillary | BPX-5 | 30. | 426. | Aflalaye, Sternberg, et al., 1995 | 12. m/0.15 mm/0.25 μm, H2 |
Capillary | CP Sil 5 CB | 20. | 425. | Do and Raulin, 1992 | 25. m/0.15 mm/2. μm, H2 |
Capillary | Squalane | 50. | 417.0 | Papazova, Milina, et al., 1988 | Column length: 50. m; Column diameter: 0.25 mm |
Capillary | DB-1 | 40. | 425. | Lubeck and Sutton, 1984 | 60. m/0.264 mm/0.25 μm, H2 |
Capillary | HP-PONA | 40. | 425. | Lubeck and Sutton, 1984 | 50. m/0.21 mm/0.5 μm, H2 |
Capillary | OV-1 | 20. | 418. | Nijs and Jacobs, 1981 | He; Column length: 150. m; Column diameter: 0.50 mm |
Capillary | Squalane | 50. | 416.5 | Bajus, Veselý, et al., 1979 | Column length: 100. m; Column diameter: 0.25 mm |
Capillary | Squalane | 70. | 416.5 | Bajus, Veselý, et al., 1979 | Column length: 100. m; Column diameter: 0.25 mm |
Capillary | Squalane | 50. | 416.3 | Bajus, Veselý, et al., 1979, 2 | Column length: 100. m; Column diameter: 0.25 mm |
Capillary | Squalane | 70. | 416.5 | Bajus, Veselý, et al., 1979, 2 | Column length: 100. m; Column diameter: 0.25 mm |
Capillary | Squalane | 50. | 416.85 | Pacáková and Koslík, 1978 | 50. m/0.2 mm/0.5 μm, N2 |
Packed | Squalane | 80. | 417. | Chrétien and Dubois, 1977 | |
Capillary | Squalane | 50. | 417. | Chretien and Dubois, 1976 | |
Capillary | Squalane | 100. | 427.3 | Lulova, Leont'eva, et al., 1976 | He; Column length: 120. m; Column diameter: 0.25 mm |
Capillary | Squalane | 50. | 417. | Rijks and Cramers, 1974 | N2; Column length: 100. m; Column diameter: 0.25 mm |
Capillary | Squalane | 70. | 417. | Rijks and Cramers, 1974 | N2; Column length: 100. m; Column diameter: 0.25 mm |
Capillary | Squalane | 40. | 411. | Matukuma, 1969 | N2; Column length: 91.4 m; Column diameter: 0.25 mm |
Packed | Squalane | 27. | 416. | Hively and Hinton, 1968 | He, Chromosorb P; Column length: 15. m; Column diameter: 0.25 mm |
Packed | Squalane | 49. | 417. | Hively and Hinton, 1968 | He, Chromosorb P; Column length: 15. m; Column diameter: 0.25 mm |
Packed | Squalane | 67. | 417. | Hively and Hinton, 1968 | He, Chromosorb P; Column length: 15. m; Column diameter: 0.25 mm |
Packed | Squalane | 86. | 418. | Hively and Hinton, 1968 | He, Chromosorb P; Column length: 15. m; Column diameter: 0.25 mm |
Packed | SE-30 | 70. | 427. | Widmer, 1967 | Diatoport S; Column length: 7.9 m |
Packed | SE-30 | 70. | 427. | Widmer, 1967 | Diatoport S; Column length: 7.9 m |
Kovats' RI, non-polar column, custom temperature program
Column type | Active phase | I | Reference | Comment |
---|---|---|---|---|
Capillary | Petrocol DH-100 | 428.2 | Haagen-Smit Laboratory, 1997 | He; Column length: 100. m; Column diameter: 0.2 mm; Program: 5C(10min) => 5C/min => 50C(48min) => 1.5C/min => 195C(91min) |
Kovats' RI, polar column, isothermal
Column type | Active phase | Temperature (C) | I | Reference | Comment |
---|---|---|---|---|---|
Packed | Carbowax 20M | 130. | 481. | Widmer, 1967 | Diatoport P; Column length: 7.9 m |
Packed | Carbowax 20M | 70. | 468. | Widmer, 1967 | Diatoport P; Column length: 7.9 m |
Packed | Carbowax 20M | 70. | 468. | Widmer, 1967 | Diatoport P; Column length: 7.9 m |
Van Den Dool and Kratz RI, non-polar column, temperature ramp
Column type | Active phase | I | Reference | Comment |
---|---|---|---|---|
Capillary | Ultra-1 | 420. | Olson, Sinkevitch, et al., 1992 | 4. K/min; Tstart: -40. C; Tend: 230. C |
Capillary | Petrocol DH | 416.44 | White, Douglas, et al., 1992 | 100. m/0.25 mm/0.5 μm, He, 1. K/min; Tstart: 30. C; Tend: 220. C |
Capillary | Petrocol DH | 418.18 | White, Douglas, et al., 1992 | 100. m/0.25 mm/0.5 μm, He, 1. K/min; Tstart: 30. C; Tend: 220. C |
Van Den Dool and Kratz RI, non-polar column, custom temperature program
Column type | Active phase | I | Reference | Comment |
---|---|---|---|---|
Capillary | DB-5 | 411. | Zaikin and Borisov, 2002 | He; Column length: 30. m; Column diameter: 0.25 mm; Program: 30C => 5K/min=120C => 10C/min => 270C |
Normal alkane RI, non-polar column, isothermal
Column type | Active phase | Temperature (C) | I | Reference | Comment |
---|---|---|---|---|---|
Capillary | OV-101 | 40. | 417. | Li and Deng, 1998 | N2; Column length: 51. m; Column diameter: 0.25 mm |
Capillary | Methyl Silicone | 50. | 417. | N/A | N2; Column length: 74.6 m; Column diameter: 0.28 mm |
Packed | Methyl Silicone | 50. | 431. | Huguet, 1961 | Nitrogen, Celite C-22; Column length: 2.5 m |
Normal alkane RI, non-polar column, temperature ramp
Column type | Active phase | I | Reference | Comment |
---|---|---|---|---|
Capillary | Polydimethyl siloxane: CP-Sil 5 CB | 422. | Bramston-Cook, 2013 | 60. m/0.25 mm/1.0 μm, Helium, 45. C @ 1.45 min, 3.6 K/min, 210. C @ 2.72 min |
Capillary | Petrocol DH | 426. | Supelco, 2012 | 100. m/0.25 mm/0.50 μm, Helium, 20. C @ 15. min, 15. K/min, 220. C @ 30. min |
Capillary | PONA | 416. | Zhang, Ding, et al., 2009 | 50. m/0.20 mm/0.50 μm, Nitrogen, 35. C @ 15. min, 2. K/min, 200. C @ 10. min |
Capillary | OV-101 | 420. | Chupalov and Zenkevich, 1996 | N2, 3. K/min; Column length: 52. m; Column diameter: 0.26 mm; Tstart: 50. C; Tend: 220. C |
Capillary | SE-54 | 416. | Guan, Li, et al., 1995 | 60. C @ 2. min, 4. K/min; Column length: 50. m; Column diameter: 0.32 mm; Tend: 200. C |
Capillary | DB-1 | 416. | Ciccioli, Cecinato, et al., 1992 | 60. m/0.32 mm/1.2 μm, He, 30. C @ 10. min, 3. K/min; Tend: 240. C |
Normal alkane RI, non-polar column, custom temperature program
Column type | Active phase | I | Reference | Comment |
---|---|---|---|---|
Capillary | Polydimethyl siloxane | 417. | Junkes, Castanho, et al., 2003 | Program: not specified |
Capillary | PONA | 428. | Perkin Elmer Instruments, 2002 | Column length: 100. m; Phase thickness: 0.50 μm; Program: not specified |
Capillary | Methyl Silicone | 421. | Spieksma, 1999 | Program: not specified |
Capillary | Polydimethyl siloxanes | 420. | Zenkevich, Chupalov, et al., 1996 | Program: not specified |
Packed | SE-30 | 427. | Robinson and Odell, 1971 | N2, Chromosorb W; Column length: 6.1 m; Program: 50C910min) => 20C/min => 90(6min) => 10C/min => 150C(hold) |
Packed | Squalane | 428. | Robinson and Odell, 1971 | N2, Embacel; Column length: 3.0 m; Program: 25C(5min) => 2C/min => 35 => 4C/min => 95C(hold) |
References
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Gas Chromatography, 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]
Scott R.B., 1944
Scott R.B.,
Thermodynamic properties of cis-2-butene from 15 to 1500 K,
J. Res. Nat. Bur. Stand., 1944, 33, 1-20. [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]
Kistiakowsky G.B., 1940
Kistiakowsky G.B.,
Gaseous heat capacities. III,
J. Chem. Phys., 1940, 8, 618-622. [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]
Scott, Ferguson, et al., 1944
Scott, R.B.; Ferguson, W.J.; Brickwedde, F.G.,
Thermodynamic properties of cis-2-butene from 15° to 1,500 K,
J. Res. NBS, 1944, 33, 1-20. [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]
Schlinger and Sage, 1952
Schlinger, W.G.; Sage, B.H.,
Isobaric heat capacities at bubble point. cis-2-butene, isopropylbenzene, and n-decane,
Ind. Eng. Chem., 1952, 44, 2454-2456. [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, 876-82. [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]
Todd and Parks, 1936, 2
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. [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]
Ambrose, Cox, et al., 1960
Ambrose, D.; Cox, J.D.; Townsend, R.,
The critical temperatures of forty organic compounds,
Trans. Faraday Soc., 1960, 56, 1452. [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]
Scott, Ferguson, et al., 1944, 2
Scott, R.B.; Ferguson, W.J.; Brickwedde, F.G.,
Thermodynamic properties of cis-2-butene from 15 degrees to 1,500 degrees K,
J. RES. NATL. BUR. STAN., 1944, 33, 1, 1-17, https://doi.org/10.6028/jres.033.001
. [all data]
Kistiakowsky, Ruhoff, et al., 1935, 2
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]
Hopkins, 1921
Hopkins, O.P.,
THE CHEMICAL INDUSTRY AND TRADE OF ENGLAND.,
J. Ind. Eng. Chem., 1921, 13, 3, 189-197, https://doi.org/10.1021/ie50135a007
. [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]
Domalski and Hearing, 1996
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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 Tfus Fusion (melting) point Ttriple Triple point temperature Vc Critical volume 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 ΔrH° Enthalpy of reaction at standard conditions ΔvapH Enthalpy of vaporization ΔvapH° Enthalpy of vaporization at standard conditions ρc Critical density - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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