Cyclohexene
- Formula: C6H10
- Molecular weight: 82.1436
- IUPAC Standard InChIKey: HGCIXCUEYOPUTN-UHFFFAOYSA-N
- CAS Registry Number: 110-83-8
- 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. - Other names: Benzene tetrahydride; Benzene, tetrahydro-; Cyclohex-1-ene; Tetrahydrobenzene; 1,2,3,4-Tetrahydrobenzene; Cykloheksen; Hexanaphthylene; UN 2256; 1-Cyclohexene; NSC 24835
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Gas phase thermochemistry data
Go To: Top, 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 as indicated in comments:
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
DRB - Donald R. Burgess, Jr.
GT - Glushko Thermocenter, Russian Academy of Sciences, Moscow
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°gas | -4.32 ± 0.98 | kJ/mol | Ccr | Steele, Chirico, et al., 1996 | ALS |
ΔfH°gas | -4.7 | kJ/mol | N/A | Good and Smith, 1969 | Value computed using ΔfHliquid° value of -38.2±0.6 kj/mol from Good and Smith, 1969 and ΔvapH° value of 33.5 kj/mol from Steele, Chirico, et al., 1996.; DRB |
ΔfH°gas | -5.3 | kJ/mol | N/A | Labbauf and Rossini, 1961 | Value computed using ΔfHliquid° value of -38.8±0.6 kj/mol from Labbauf and Rossini, 1961 and ΔvapH° value of 33.5 kj/mol from Steele, Chirico, et al., 1996.; DRB |
ΔfH°gas | -7.1 | kJ/mol | N/A | Epstein, Pitzer, et al., 1949 | Value computed using ΔfHliquid° value of -40.6±0.8 kj/mol from Epstein, Pitzer, et al., 1949 and ΔvapH° value of 33.5 kj/mol from Steele, Chirico, et al., 1996.; DRB |
Quantity | Value | Units | Method | Reference | Comment |
S°gas | 310.45 | J/mol*K | N/A | Beckett C.W., 1948 | GT |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
35.12 | 50. | Dorofeeva O.V., 1986 | Recommended S(298.15 K) value agrees well with experimental one [ Beckett C.W., 1948], however calculated Cp(T) values are about 5 J/mol*K lower than those obtained from experimental measurements [ Montgomery J.B., 1942]. To fit calculated Cp(T) values to experiment, [ Beckett C.W., 1948] suggested existence of stable half-boat conformation. This suggestion was found to be incorrect later. [ Dorofeeva O.V., 1986] used more reliable data on molecular structure and their S(T) and Cp(T) values are in good agreement with results of detail force-field calculations [ Lenz T.G., 1990].; GT |
43.06 | 100. | ||
53.78 | 150. | ||
67.35 | 200. | ||
92.14 | 273.15 | ||
101.5 ± 3.0 | 298.15 | ||
102.16 | 300. | ||
139.70 | 400. | ||
173.27 | 500. | ||
201.44 | 600. | ||
224.91 | 700. | ||
244.65 | 800. | ||
261.38 | 900. | ||
275.63 | 1000. | ||
287.83 | 1100. | ||
298.29 | 1200. | ||
307.29 | 1300. | ||
315.06 | 1400. | ||
321.78 | 1500. |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
133.47 | 370. | Montgomery J.B., 1942 | GT |
141.42 | 390. | ||
148.53 | 410. |
Condensed phase thermochemistry data
Go To: Top, Gas 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 as indicated in comments:
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 |
---|---|---|---|---|---|
ΔfH°liquid | -37.8 ± 8.2 | kJ/mol | Ccr | Steele, Chirico, et al., 1996 | ALS |
ΔfH°liquid | -38.2 ± 0.59 | kJ/mol | Ccb | Good and Smith, 1969 | ALS |
ΔfH°liquid | -38.8 ± 0.59 | kJ/mol | Ccb | Labbauf and Rossini, 1961 | ALS |
ΔfH°liquid | -40.6 ± 0.79 | kJ/mol | Ccb | Epstein, Pitzer, et al., 1949 | Unpublished results; ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -3752.39 ± 0.49 | kJ/mol | Ccr | Steele, Chirico, et al., 1996 | Corresponding ΔfHºliquid = -37.82 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -3752.0 ± 0.50 | kJ/mol | Ccb | Good and Smith, 1969 | Corresponding ΔfHºliquid = -38.2 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -3751.5 ± 0.50 | kJ/mol | Ccb | Labbauf and Rossini, 1961 | Corresponding ΔfHºliquid = -38.7 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -3761. | kJ/mol | Ccb | Konovalon, 1926 | Heat of combustion at 15°C; Corresponding ΔfHºliquid = -30. kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
Quantity | Value | Units | Method | Reference | Comment |
S°liquid | 214.60 | J/mol*K | N/A | Haida, Suga, et al., 1977 | DH |
S°liquid | 216.19 | J/mol*K | N/A | Huffman, Eaton, et al., 1948 | DH |
S°liquid | 216.7 | J/mol*K | N/A | Parks and Huffman, 1930 | Extrapolation below 90 K, 49.20 J/mol*K.; DH |
Constant pressure heat capacity of liquid
Cp,liquid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
148.8 | 298.15 | Steele, Chirico, et al., 1993 | DH |
152.90 | 298.12 | Kalinowska and Woycicki, 1988 | T = 183 to 298 K. Unsmoothed experimental datum.; DH |
148.35 | 298.15 | Haida, Suga, et al., 1977 | T = 15 to 293 K.; DH |
149.16 | 298.15 | Huffman, Eaton, et al., 1948 | T = 12 to 300 K.; DH |
145.6 | 293.2 | Parks and Huffman, 1930 | T = 92 to 293 K. Value is unsmoothed experimental datum.; DH |
Phase change data
Go To: Top, Gas phase thermochemistry data, Condensed 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
BS - Robert L. Brown and Stephen E. Stein
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
DRB - Donald R. Burgess, Jr.
AC - William E. Acree, Jr., James S. Chickos
CAL - James S. Chickos, William E. Acree, Jr., Joel F. Liebman, Students of Chem 202 (Introduction to the Literature of Chemistry), University of Missouri -- St. Louis
DH - Eugene S. Domalski and Elizabeth D. Hearing
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 356. ± 2. | K | AVG | N/A | Average of 56 out of 57 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 169. ± 1. | K | AVG | N/A | Average of 9 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 169.66 | K | N/A | Haida, Suga, et al., 1977, 2 | Crystal phase 1 phase; Uncertainty assigned by TRC = 0.02 K; TRC |
Ttriple | 169.67 | K | N/A | Huffman, Eaton, et al., 1948, 2 | Crystal phase 1 phase; Uncertainty assigned by TRC = 0.05 K; TRC |
Ttriple | 169.0 | K | N/A | Parks and Huffman, 1930, 2 | Crystal phase 1 phase; Uncertainty assigned by TRC = 0.2 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 560.4 ± 0.1 | K | N/A | Tsonopoulos and Ambrose, 1996 | |
Tc | 560.4 | K | N/A | Majer and Svoboda, 1985 | |
Tc | 560.4 | K | N/A | Cheng, McCoubrey, et al., 1962 | Uncertainty assigned by TRC = 0.3 K; Visual (5-cm 2-mm bore tubes) in nitrate-nitrite bath, TE or TH cal. vs NPL thermometer; TRC |
Tc | 560.42 | K | N/A | Ambrose, Cox, et al., 1960 | Uncertainty assigned by TRC = 0.02 K; Visual, PRT, IPTS-48, with decomp.; TRC |
Tc | 553.5 | K | N/A | Ambrose and Grant, 1957 | Uncertainty assigned by TRC = 0.15 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 33.57 | kJ/mol | N/A | Majer and Svoboda, 1985 | |
ΔvapH° | 33.50 ± 0.53 | kJ/mol | V | Steele, Chirico, et al., 1996 | ALS |
ΔvapH° | 33.5 | kJ/mol | N/A | Steele, Chirico, et al., 1996 | DRB |
ΔvapH° | 33.5 ± 0.5 | kJ/mol | EB | Steele, Chirico, et al., 1996 | Based on data from 285. to 357. K.; AC |
ΔvapH° | 30.5 ± 0.3 | kJ/mol | V | Mathews, 1926 | ALS |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
30.46 | 356.2 | N/A | Majer and Svoboda, 1985 | |
32.8 | 330. | N/A | Marrufo, Aucejo, et al., 2009 | Based on data from 315. to 356. K.; AC |
32.9 | 325. | N/A | Steyer and Sundmacher, 2004 | Based on data from 310. to 356. K.; AC |
32.6 | 327. | N/A | Segura, Lam, et al., 2001 | Based on data from 312. to 356. K.; AC |
32.7 | 324. | A,EB | Stephenson and Malanowski, 1987 | Based on data from 309. to 365. K. See also Meyer and Hotz, 1973.; AC |
33.1 | 308. | MM | Letcher and Marsicano, 1974 | Based on data from 305. to 322. K.; AC |
32.7 ± 0.1 | 313. | C | Svoboda, Veselý, et al., 1973 | AC |
32.2 ± 0.1 | 323. | C | Svoboda, Veselý, et al., 1973 | AC |
31.7 ± 0.1 | 333. | C | Svoboda, Veselý, et al., 1973 | AC |
31.2 ± 0.1 | 343. | C | Svoboda, Veselý, et al., 1973 | AC |
30.7 ± 0.1 | 353. | C | Svoboda, Veselý, et al., 1973 | AC |
33.7 | 300. | MM | Forziati, Camin, et al., 1950 | Based on data from 285. to 357. K.; AC |
32.59 | 300. | V | Lister, 1941 | Heat of bromination at 300 K; ALS |
32.6 | 300. | N/A | Lister, 1941 | Based on data from 229. to 292. K.; 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 |
---|---|---|---|---|---|
313. to 353. | 47.19 | 0.2662 | 560.4 | 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 |
---|---|---|---|---|
310.02 to 364.53 | 3.9973 ± 0.0018 | 1221.9 ± 1.0 | -49.98 ± 0.12 | Meyer and Hotz, 1973 |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
3.28 | 169.7 | Domalski and Hearing, 1996 | AC |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
30.5 | 138.7 | Domalski and Hearing, 1996 | CAL |
19.35 | 169.7 |
Enthalpy of phase transition
ΔHtrs (kJ/mol) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
1.483 | 112.3 | crystaline, III | crystaline, I | Haida, Suga, et al., 1977 | DH |
4.231 | 138.63 | crystaline, II | crystaline, I | Haida, Suga, et al., 1977 | DH |
3.284 | 169.66 | crystaline, I | liquid | Haida, Suga, et al., 1977 | DH |
4.2505 | 138.7 | crystaline, II | crystaline, I | Huffman, Eaton, et al., 1948 | DH |
3.2932 | 169.67 | crystaline, I | liquid | Huffman, Eaton, et al., 1948 | DH |
4.075 | 138.7 | crystaline, II | crystaline, I | Parks and Huffman, 1930 | DH |
3.289 | 169.0 | crystaline, I | liquid | Parks and Huffman, 1930 | DH |
Entropy of phase transition
ΔStrs (J/mol*K) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
13.2 | 112.3 | crystaline, III | crystaline, I | Haida, Suga, et al., 1977 | DH |
30.52 | 138.63 | crystaline, II | crystaline, I | Haida, Suga, et al., 1977 | DH |
19.36 | 169.66 | crystaline, I | liquid | Haida, Suga, et al., 1977 | DH |
30.65 | 138.7 | crystaline, II | crystaline, I | Huffman, Eaton, et al., 1948 | DH |
19.41 | 169.67 | crystaline, I | liquid | Huffman, Eaton, et al., 1948 | DH |
29.38 | 138.7 | crystaline, II | crystaline, I | Parks and Huffman, 1930 | DH |
19.46 | 169.0 | crystaline, I | liquid | Parks and Huffman, 1930 | DH |
References
Go To: Top, Gas phase thermochemistry data, Condensed 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.
Steele, Chirico, et al., 1996
Steele, W.V.; Chirico, R.D.; Knipmeyer, S.E.; Nguyen, A.; Smith, N.K.; Tasker, I.R.,
Thermodynamic properties and ideal-gas enthalpies of formation for cyclohexene, phthalan (2,5-dihydrobenzo-3,4-furan), isoxazole, octylamine, dioctylamine, trioctylamine, phenyl isocyanate, and 1,4,5,6-tetrahydropyrimidine,
J. Chem. Eng. Data, 1996, 41, 1269-1284. [all data]
Good and Smith, 1969
Good, W.D.; Smith, N.K.,
Enthalpies of combustion of toluene, benzene, cyclohexane, cyclohexene, methylcyclopentane, 1-methylcyclopentene, and n-hexane,
J. Chem. Eng. Data, 1969, 14, 102-106. [all data]
Labbauf and Rossini, 1961
Labbauf, A.; Rossini, F.D.,
Heats of combustion, formation, and hydrogenation of 14 selected cyclomonoolefin hydrocarbons,
J. Phys. Chem., 1961, 65, 476-480. [all data]
Epstein, Pitzer, et al., 1949
Epstein, M.B.; Pitzer, K.S.; Rossini, F.D.,
Heats, equilibrium constants, and free energies of formation of cyclopentene and cyclohexene,
J. Res. NBS, 1949, 42, 379-382. [all data]
Beckett C.W., 1948
Beckett C.W.,
The thermodynamic properties and molecular structure of cyclopentene and cyclohexene,
J. Am. Chem. Soc., 1948, 70, 4227-4230. [all data]
Dorofeeva O.V., 1986
Dorofeeva O.V.,
Thermodynamic properties of twenty-one monocyclic hydrocarbons,
J. Phys. Chem. Ref. Data, 1986, 15, 437-464. [all data]
Montgomery J.B., 1942
Montgomery J.B.,
The heat capacity of organic vapors. IV. Benzene, fluorobenzene, toluene, cyclohexane, methylcyclohexane and cyclohexene,
J. Am. Chem. Soc., 1942, 64, 2375-2377. [all data]
Lenz T.G., 1990
Lenz T.G.,
Force field calculation of equilibrium thermodynamic properties: Diels-Alder reaction of 1,3-butadiene and ethylene and Diels-Alder dimerization of 1,3-butadiene,
J. Comput. Chem., 1990, 11, 351-360. [all data]
Konovalon, 1926
Konovalon, D.-P.,
Sur Les Chaleurs de Combustion de Quelques hydrocarbures cycliques,
J. Chim. Phys., 1926, 23, 359-362. [all data]
Haida, Suga, et al., 1977
Haida, O.; Suga, H.; Seki, S.,
Calorimetric study of the glassy state. XI. Plural glass-transition phenomena of cyclohexene,
Bull. Chem. Soc. Japan, 1977, 50, 802-809. [all data]
Huffman, Eaton, et al., 1948
Huffman, H.M.; Eaton, M.; Oliver, G.D.,
The heat capacities, heats of transition, heats of fusion and entropies of cyclopentene and cyclohexene,
J. Am. Chem. Soc., 1948, 70, 2911-2914. [all data]
Parks and Huffman, 1930
Parks, G.S.; Huffman, H.M.,
Thermal data on organic compounds. IX. A study of the effect of unsaturation on the heat capacities, entropies and free energies of some hydrocarbons and other compounds,
J. Am. Chem. Soc., 1930, 52, 4381-4391. [all data]
Steele, Chirico, et al., 1993
Steele, W.V.; Chirico, R.D.; Knipmeyer, S.E.; Nguyen, A.; Tasker, I.R.,
Determination of ideal gas enthalpies of formation for key compounds the 1991 project results,
DIPPR Project, 1993, 871, NIPER-716. [all data]
Kalinowska and Woycicki, 1988
Kalinowska, B.; Woycicki, W.,
Heat capacities and excess heat capacities of (an alkanol + an unsaturated hydrocarbon). II. (Propan-1-ol + cyclohexene),
J. Chem. Thermodynam., 1988, 20, 1131-1135. [all data]
Haida, Suga, et al., 1977, 2
Haida, O.; Suga, H.; Seki, S.,
Calorimetric study of the glassy state. XI. Plural glass transition phenomena of cyclohexene,
Bull. Chem. Soc. Jpn., 1977, 50, 802. [all data]
Huffman, Eaton, et al., 1948, 2
Huffman, H.M.; Eaton, M.; Oliver, G.D.,
The heat capacities, heats of transition, heats of fusion and entropies of cyclopentene and cyclohexene,
J. Am. Chem. Soc., 1948, 70, 2911. [all data]
Parks and Huffman, 1930, 2
Parks, G.S.; Huffman, H.M.,
Thermal data on organic compounds. IX. A study of the effect of unsaturation on the heat capacities, entropies and free energies of some hydrocarbons and other compounds,
J. Am. Chem. Soc., 1930, 52, 4381. [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]
Cheng, McCoubrey, et al., 1962
Cheng, D.C.H.; McCoubrey, J.C.; Phillips, D.G.,
Critical Temperatures of Some Organic Cyclic Compounds,
Trans. Faraday Soc., 1962, 58, 224. [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]
Ambrose and Grant, 1957
Ambrose, D.; Grant, D.G.,
The Critical Temperatures of Some Hydrocarbons and Pyridine Bases,
Trans. Faraday Soc., 1957, 53, 771. [all data]
Mathews, 1926
Mathews, J.H.,
The accurate measurement of heats of vaporization of liquids,
J. Am. Chem. Soc., 1926, 48, 562-576. [all data]
Marrufo, Aucejo, et al., 2009
Marrufo, Beatriz; Aucejo, Antonio; Sanchotello, Margarita; Loras, Sonia,
Isobaric vapor--liquid equilibrium for binary mixtures of 1-hexene+n-hexane and cyclohexane+cyclohexene at 30, 60 and 101.3kPa,
Fluid Phase Equilibria, 2009, 279, 1, 11-16, https://doi.org/10.1016/j.fluid.2008.12.007
. [all data]
Steyer and Sundmacher, 2004
Steyer, Frank; Sundmacher, Kai,
VLE and LLE Data for the System Cyclohexane + Cyclohexene + Water + Cyclohexanol,
J. Chem. Eng. Data, 2004, 49, 6, 1675-1681, https://doi.org/10.1021/je049902w
. [all data]
Segura, Lam, et al., 2001
Segura, Hugo; Lam, Elizabeth; Reich, Ricardo; Wisniak, Jaime,
Isobaric Phase Equilibria in the Binary Systems Ethyl 1,1-Dimethylethyl Ether + 1-hexene and + Cyclohexene at 94.00 kPa,
Physics and Chemistry of Liquids, 2001, 39, 1, 43-54, https://doi.org/10.1080/00319100108030325
. [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]
Meyer and Hotz, 1973
Meyer, Edwin F.; Hotz, Roger D.,
High-precision vapor-pressure data for eight organic compounds,
J. Chem. Eng. Data, 1973, 18, 4, 359-362, https://doi.org/10.1021/je60059a008
. [all data]
Letcher and Marsicano, 1974
Letcher, T.M.; Marsicano, F.,
Vapour pressures and densities of some unsaturated C6 acyclic and cyclic hydrocarbons between 300 and 320 K,
The Journal of Chemical Thermodynamics, 1974, 6, 5, 509-514, https://doi.org/10.1016/0021-9614(74)90013-5
. [all data]
Svoboda, Veselý, et al., 1973
Svoboda, V.; Veselý, F.; Holub, R.; Pick, J.,
Enthalpy data of liquids. II. The dependence of heats of vaporization of methanol, propanol, butanol, cyclohexane, cyclohexene, and benzene on temperature,
Collect. Czech. Chem. Commun., 1973, 38, 12, 3539-3543, https://doi.org/10.1135/cccc19733539
. [all data]
Forziati, Camin, et al., 1950
Forziati, A.F.; Camin, D.L.; Rossini, F.D.,
Density, refractive index, boiling point, and vapor pressure of eight monoolefin (1-alkene), six pentadiene, and two cyclomonoolefin hydrocarbons,
J. RES. NATL. BUR. STAN., 1950, 45, 5, 406, https://doi.org/10.6028/jres.045.044
. [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]
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, Condensed phase thermochemistry data, Phase change data, References
- Symbols used in this document:
Cp,gas Constant pressure heat capacity of gas Cp,liquid Constant pressure heat capacity of liquid S°gas Entropy of gas at standard conditions S°liquid Entropy of liquid at standard conditions Tboil Boiling point Tc Critical temperature Tfus Fusion (melting) point Ttriple Triple point temperature ΔHtrs Enthalpy of phase transition ΔStrs Entropy of phase transition 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 ΔfusH Enthalpy of fusion ΔfusS Entropy of fusion ΔvapH Enthalpy of vaporization ΔvapH° Enthalpy of vaporization at standard conditions - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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