Benzene
- Formula: C6H6
- Molecular weight: 78.1118
- IUPAC Standard InChIKey: UHOVQNZJYSORNB-UHFFFAOYSA-N
- CAS Registry Number: 71-43-2
- 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. - Isotopologues:
- Other names: [6]Annulene; Benzol; Benzole; Coal naphtha; Cyclohexatriene; Phenyl hydride; Pyrobenzol; Pyrobenzole; Benzolene; Bicarburet of hydrogen; Carbon oil; Mineral naphtha; Motor benzol; Benzeen; Benzen; Benzin; Benzine; Benzolo; Fenzen; NCI-C55276; Phene; Rcra waste number U019; UN 1114; NSC 67315; 1,3,5-Cyclohexatriene
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Gas phase thermochemistry data
Go To: Top, 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:
DRB - Donald R. Burgess, Jr.
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 | 82.9 ± 0.9 | kJ/mol | Review | Roux, Temprado, et al., 2008 | There are sufficient high-quality literature values to make a good evaluation with a high degree of confidence. In general, the evaluated uncertainty limits are on the order of (0.5 to 2.5) kJ/mol.; DRB |
ΔfH°gas | 82.8 | kJ/mol | N/A | Good and Smith, 1969 | Value computed using ΔfHliquid° value of 49.0±0.5 kj/mol from Good and Smith, 1969 and ΔvapH° value of 33.9 kj/mol from Prosen, Gilmont, et al., 1945.; DRB |
ΔfH°gas | 82.93 ± 0.50 | kJ/mol | Ccb | Prosen, Gilmont, et al., 1945 | Hf by Prosen, Johnson, et al., 1946; ALS |
ΔfH°gas | 79.9 | kJ/mol | N/A | Landrieu, Baylocq, et al., 1929 | Value computed using ΔfHliquid° value of 46.0 kj/mol from Landrieu, Baylocq, et al., 1929 and ΔvapH° value of 33.9 kj/mol from Prosen, Gilmont, et al., 1945.; DRB |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
33.27 | 50. | Thermodynamics Research Center, 1997 | GT |
35.11 | 100. | ||
41.94 | 150. | ||
53.17 | 200. | ||
74.55 | 273.15 | ||
82.44 | 298.15 | ||
83.02 | 300. | ||
113.52 | 400. | ||
139.35 | 500. | ||
160.09 | 600. | ||
176.78 | 700. | ||
190.45 | 800. | ||
201.82 | 900. | ||
211.41 | 1000. | ||
219.56 | 1100. | ||
226.52 | 1200. | ||
232.49 | 1300. | ||
237.65 | 1400. | ||
242.11 | 1500. | ||
250.91 | 1750. | ||
257.26 | 2000. | ||
261.95 | 2250. | ||
265.50 | 2500. | ||
268.23 | 2750. | ||
270.37 | 3000. |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
93.32 ± 0.06 | 333.15 | Todd S.S., 1978 | Please also see Montgomery J.B., 1942, Pitzer K.S., 1943, Scott D.W., 1947.; GT |
95.81 | 341.60 | ||
97.99 ± 0.06 | 348.15 | ||
103.98 ± 0.06 | 368.15 | ||
105.02 | 370. | ||
104.77 | 371.20 | ||
108.8 ± 1.3 | 388. | ||
110.88 | 390. | ||
110.5 ± 1.3 | 393. | ||
113.93 | 402.30 | ||
114.29 ± 0.07 | 403.15 | ||
115.48 | 410. | ||
117.6 ± 1.3 | 417. | ||
118.8 ± 1.3 | 428. | ||
123.39 | 436.15 | ||
123.93 ± 0.07 | 438.15 | ||
126.8 ± 1.3 | 463. | ||
132.42 | 471.10 | ||
132.94 ± 0.08 | 473.15 | ||
131.4 ± 1.3 | 481. | ||
139.47 ± 0.08 | 500.15 | ||
145.59 ± 0.09 | 527.15 |
Phase change data
Go To: Top, Gas 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:
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, Chris Muzny director
BS - Robert L. Brown and Stephen E. Stein
DRB - Donald R. Burgess, Jr.
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
AC - William E. Acree, Jr., James S. Chickos
DH - Eugene S. Domalski and Elizabeth D. Hearing
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 353.3 ± 0.1 | K | AVG | N/A | Average of 147 out of 183 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 278.64 ± 0.08 | K | AVG | N/A | Average of 57 out of 69 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 278.5 ± 0.6 | K | AVG | N/A | Average of 9 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 562.0 ± 0.8 | K | AVG | N/A | Average of 36 out of 41 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 48.9 ± 0.4 | bar | AVG | N/A | Average of 24 out of 26 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Vc | 0.25 ± 0.03 | l/mol | AVG | N/A | Average of 6 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 3.9 ± 0.2 | mol/l | AVG | N/A | Average of 12 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 33.9 ± 0.1 | kJ/mol | AVG | N/A | Average of 10 out of 11 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ΔsubH° | 44.4 | kJ/mol | TE,ME | Kruif, 1980 | Based on data from 183. to 197. K.; AC |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
30.72 | 353.3 | N/A | Majer and Svoboda, 1985 | |
33.2 | 320. | N/A | Lubomska, Banas, et al., 2002 | Based on data from 305. to 345. K.; AC |
35.6 | 258. to 313. | GC | Liu and Dickhut, 1994 | AC |
33.5 | 311. | EB | Ambrose, Ewing, et al., 1990 | Based on data from 296. to 377. K.; AC |
33.4 | 307. | C | Dong, Lin, et al., 1988 | AC |
33.1 | 314. | C | Dong, Lin, et al., 1988 | AC |
32.4 | 324. | C | Dong, Lin, et al., 1988 | AC |
31.9 | 332. | C | Dong, Lin, et al., 1988 | AC |
31.4 | 344. | C | Dong, Lin, et al., 1988 | AC |
30.6 | 353. | C | Dong, Lin, et al., 1988 | AC |
34.4 | 294. | A | Stephenson and Malanowski, 1987 | Based on data from 279. to 377. K.; AC |
31.5 | 368. | A | Stephenson and Malanowski, 1987 | Based on data from 353. to 422. K.; AC |
30.2 | 435. | A | Stephenson and Malanowski, 1987 | Based on data from 420. to 502. K.; AC |
30.3 | 516. | A | Stephenson and Malanowski, 1987 | Based on data from 501. to 562. K.; AC |
30.8 | 352. | N/A | Natarajan, 1983 | AC |
30.5 | 361. | N/A | Natarajan, 1983 | AC |
30.2 | 366. | N/A | Natarajan, 1983 | AC |
35.3 | 343. | N/A | Tsonopoulos and Wilson, 1983 | Based on data from 313. to 373. K.; AC |
31. | 350. | N/A | Rao and Viswanath, 1977 | AC |
33.0 ± 0.1 | 313. | C | Svoboda, Veselý, et al., 1973 | AC |
32.2 ± 0.1 | 328. | C | Svoboda, Veselý, et al., 1973 | AC |
31.8 ± 0.1 | 333. | C | Svoboda, Veselý, et al., 1973 | AC |
31.4 ± 0.1 | 343. | C | Svoboda, Veselý, et al., 1973 | AC |
30.9 ± 0.1 | 353. | C | Svoboda, Veselý, et al., 1973 | AC |
32.6 ± 0.4 | 313. | DSC | Mita, Imai, et al., 1971 | AC |
32.5 ± 0.5 | 328. | DSC | Mita, Imai, et al., 1971 | AC |
31.6 ± 0.4 | 345. | DSC | Mita, Imai, et al., 1971 | AC |
34.1 | 299. | N/A | Forziati, Norris, et al., 1949 | Based on data from 284. to 354. K.; AC |
34.1 | 293. | N/A | Yarym-Agaev, Fedos'ev, et al., 1949 | AC |
34.1 | 297. | N/A | Thomson, 1946 | Based on data from 282. to 354. K.; AC |
31.2 | 294. | N/A | Scott and Brickwedde, 1945 | AC |
34.1 | 303. | MM | Willingham, Taylor, et al., 1945 | Based on data from 288. to 354. K.; AC |
33.4 | 313. | EB | Smith, 1941 | Based on data from 298. to 373. K.; AC |
34.5 | 288. | N/A | Stuckey and Saylor, 1940 | Based on data from 273. to 348. K.; 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) | 293. to 469. |
---|---|
A (kJ/mol) | 47.41 |
α | 0.1231 |
β | 0.3602 |
Tc (K) | 562.1 |
Reference | Majer and Svoboda, 1985 |
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 |
---|---|---|---|---|---|
333.4 to 373.5 | 4.72583 | 1660.652 | -1.461 | Eon, Pommier, et al., 1971 | Coefficents calculated by NIST from author's data. |
297.9 to 318. | 0.14591 | 39.165 | -261.236 | Deshpande and Pandya, 1967 | Coefficents calculated by NIST from author's data. |
421.56 to 554.8 | 4.60362 | 1701.073 | 20.806 | Kalafati, Rasskazov, et al., 1967 | Coefficents calculated by NIST from author's data. |
287.70 to 354.07 | 4.01814 | 1203.835 | -53.226 | Williamham, Taylor, et al., 1945 |
Enthalpy of sublimation
ΔsubH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
41.7 | 258. to 273. | N/A | Liu and Dickhut, 1994 | AC |
45.2 | 264. | A | Stephenson and Malanowski, 1987 | Based on data from 223. to 279. K. See also Ha, Morrison, et al., 1976.; AC |
45.1 | 278. | N/A | Hessler, 1984 | AC |
53.9 ± 0.8 | 193. | N/A | De Kruif and Van Ginkel, 1977 | AC |
49.4 ± 0.4 | 193. | N/A | De Kruif and Van Ginkel, 1977 | AC |
45.6 | 279. | MM | Jackowski, 1974 | Based on data from 221. to 268. K.; AC |
44.1 | 261. | N/A | Jones, 1960 | AC |
43.1 | 229. | N/A | Jones, 1960 | AC |
44.6 | 279. | N/A | Milazzo, 1956 | AC |
46.6 | 282. | A | Stull, 1947 | Based on data from 263. to 270. K.; AC |
38. | 303. | V | Wolf and Weghofer, 1938 | ALS |
44.6 | 273. | N/A | de Boer, 1936 | See also Jackowski, 1974.; AC |
43.3 | 226. | A | Mündel, 1913 | Based on data from 214. to 238. K.; AC |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
9.8663 | 278.69 | N/A | Oliver, Eaton, et al., 1948 | DH |
9.916 | 278.65 | N/A | Ziegler and Andrews, 1942 | DH |
9.87 | 278.7 | C | Domalski and Hearing, 1996 | See also Andrews, Lynn, et al., 1926 and Ziegler and Andrews, 1942.; AC |
9.300 | 279.1 | N/A | Smith, 1979 | DH |
8.950 | 278.8 | N/A | Pacor, 1967 | DH |
9.937 | 278.6 | N/A | Tschamler, 1948 | DH |
9.803 | 278.6 | N/A | Huffman, Parks, et al., 1930 | DH |
9.875 | 278.55 | N/A | Andrews, Lynn, et al., 1926 | DH |
10.000 | 278.64 | N/A | Maass and Walbauer, 1925 | DH |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
35.40 | 278.69 | Oliver, Eaton, et al., 1948 | DH |
35.59 | 278.65 | Ziegler and Andrews, 1942 | DH |
33.3 | 279.1 | Smith, 1979 | DH |
32.1 | 278.8 | Pacor, 1967 | DH |
35.19 | 278.6 | Huffman, Parks, et al., 1930 | DH |
35.5 | 278.55 | Andrews, Lynn, et al., 1926 | DH |
35.9 | 278.64 | Maass and Walbauer, 1925 | DH |
Reaction thermochemistry data
Go To: Top, Gas 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:
B - John E. Bartmess
M - Michael M. Meot-Ner (Mautner) and Sharon G. Lias
RCD - Robert C. Dunbar
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.
Reactions 1 to 50
By formula: Cl- + C6H6 = (Cl- • C6H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 25.1 ± 1.9 | kJ/mol | N/A | Tschurl, Ueberfluss, et al., 2007 | gas phase; B |
ΔrH° | 39. ± 8.4 | kJ/mol | TDAs | Hiraoka, Mizuse, et al., 1988 | gas phase; B,M |
ΔrH° | 41.4 | kJ/mol | IMRE | Larson and McMahon, 1984 | gas phase; B,M |
ΔrH° | 36. | kJ/mol | PHPMS | Paul and Kebarle, 1991 | gas phase; from Ph. D. thesis of S. Chowdhury, Entropy change calculated or estimated; M |
ΔrH° | 43.5 | kJ/mol | PHPMS | Sunner, Nishizawa, et al., 1981 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 74.9 | J/mol*K | PHPMS | Hiraoka, Mizuse, et al., 1988 | gas phase; M |
ΔrS° | 71. | J/mol*K | N/A | Paul and Kebarle, 1991 | gas phase; from Ph. D. thesis of S. Chowdhury, Entropy change calculated or estimated; M |
ΔrS° | 71.5 | J/mol*K | N/A | Larson and McMahon, 1984, 2 | gas phase; switching reaction(Cl-)t-C4H9OH, Entropy change calculated or estimated; French, Ikuta, et al., 1982; M |
ΔrS° | 92. | J/mol*K | N/A | Sunner, Nishizawa, et al., 1981 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 17. ± 11. | kJ/mol | TDAs | Hiraoka, Mizuse, et al., 1988 | gas phase; B |
ΔrG° | 16. ± 6.7 | kJ/mol | IMRE | Chowdhury and Kebarle, 1986 | gas phase; B |
ΔrG° | 20. ± 8.4 | kJ/mol | IMRE | Larson and McMahon, 1984 | gas phase; B,M |
ΔrG° | 15.9 | kJ/mol | IMRE | French, Ikuta, et al., 1982 | gas phase; B |
Free energy of reaction
ΔrG° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
15. | 300. | PHPMS | Paul and Kebarle, 1991 | gas phase; from Ph. D. thesis of S. Chowdhury, Entropy change calculated or estimated; M |
16. | 300. | PHPMS | Chowdhury and Kebarle, 1986 | gas phase; M |
16. | 300. | PHPMS | Sunner, Nishizawa, et al., 1981 | gas phase; Entropy change calculated or estimated; M |
C6H5- + =
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1678.7 ± 2.1 | kJ/mol | G+TS | Davico, Bierbaum, et al., 1995 | gas phase; Revised per Ervin and DeTuro, 2002 change in NH3 acidity. Alecu, Gao, et al., 2007 using thermal methods, agrees with this BDE: 112.8±0.6; value altered from reference due to change in acidity scale; B |
ΔrH° | 1678.5 ± 0.88 | kJ/mol | D-EA | Gunion, Gilles, et al., 1992 | gas phase; B |
ΔrH° | 1677. ± 10. | kJ/mol | TDEq | Meot-ner and Sieck, 1986 | gas phase; B |
ΔrH° | 1680. ± 42. | kJ/mol | CIDT | Graul and Squires, 1990 | gas phase; B |
ΔrH° | 1665. ± 23. | kJ/mol | G+TS | Bohme and Young, 1971 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1641.8 ± 1.7 | kJ/mol | IMRE | Davico, Bierbaum, et al., 1995 | gas phase; Revised per Ervin and DeTuro, 2002 change in NH3 acidity. Alecu, Gao, et al., 2007 using thermal methods, agrees with this BDE: 112.8±0.6; value altered from reference due to change in acidity scale; B |
ΔrG° | 1636. ± 8.4 | kJ/mol | TDEq | Meot-ner and Sieck, 1986 | gas phase; B |
ΔrG° | 1632. ± 27. | kJ/mol | IMRB | Bartmess and McIver Jr., 1979 | gas phase; B |
ΔrG° | 1628. ± 23. | kJ/mol | IMRB | Bohme and Young, 1971 | gas phase; B |
By formula: C6H6+ + C6H6 = (C6H6+ • C6H6)
Bond type: Charge transfer bond (positive ion)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 60. ± 30. | kJ/mol | AVG | N/A | Average of 7 out of 10 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 120. | J/mol*K | PHPMS | Hiraoka, Fujimaki, et al., 1991 | gas phase; M |
ΔrS° | 110. | J/mol*K | PHPMS | Meot-Ner (Mautner), Hamlet, et al., 1978 | gas phase; M |
ΔrS° | 96. | J/mol*K | HPMS | Field, Hamlet, et al., 1969 | gas phase; M |
By formula: Li+ + C6H6 = (Li+ • C6H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 161. ± 13. | kJ/mol | CIDT | Amicangelo and Armentrout, 2000 | RCD |
ΔrH° | 159. | kJ/mol | ICR | Woodin and Beauchamp, 1978 | gas phase; switching reaction(Li+)H2O, Entropy change calculated or estimated; Dzidic and Kebarle, 1970 extrapolated; M |
ΔrH° | 153. | kJ/mol | ICR | Staley and Beauchamp, 1975 | gas phase; switching reaction(Li+)H2O, from graph; Dzidic and Kebarle, 1970 extrapolated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 115. | J/mol*K | N/A | Woodin and Beauchamp, 1978 | gas phase; switching reaction(Li+)H2O, Entropy change calculated or estimated; Dzidic and Kebarle, 1970 extrapolated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 124. | kJ/mol | ICR | Woodin and Beauchamp, 1978 | gas phase; switching reaction(Li+)H2O, Entropy change calculated or estimated; Dzidic and Kebarle, 1970 extrapolated; M |
By formula: Br- + C6H6 = (Br- • C6H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 38. ± 8.4 | kJ/mol | TDAs | Hiraoka, Mizuse, et al., 1988 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 71.1 | J/mol*K | PHPMS | Hiraoka, Mizuse, et al., 1988 | gas phase; M |
ΔrS° | 71. | J/mol*K | N/A | Paul and Kebarle, 1991 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 10. ± 4.2 | kJ/mol | IMRE | Paul and Kebarle, 1991 | gas phase; B |
ΔrG° | 16. ± 11. | kJ/mol | TDAs | Hiraoka, Mizuse, et al., 1988 | gas phase; B |
Free energy of reaction
ΔrG° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
0.0 | 423. | PHPMS | Paul and Kebarle, 1991 | gas phase; Entropy change calculated or estimated; M |
By formula: (Na+ • C6H6) + C6H6 = (Na+ • 2C6H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 81. ± 5. | kJ/mol | AVG | N/A | Average of 7 values; Individual data points |
By formula: Na+ + C6H6 = (Na+ • C6H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 95.4 ± 5.9 | kJ/mol | CIDC | Amicangelo and Armentrout, 2001 | Anchor NH3=24.41; RCD |
ΔrH° | 88.3 ± 5.0 | kJ/mol | CIDT | Amicangelo and Armentrout, 2000 | RCD |
ΔrH° | 88.3 ± 4.6 | kJ/mol | CIDT | Armentrout and Rodgers, 2000 | RCD |
ΔrH° | 117. | kJ/mol | HPMS | Guo, Purnell, et al., 1990 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 131. | J/mol*K | HPMS | Guo, Purnell, et al., 1990 | gas phase; M |
Free energy of reaction
ΔrG° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
65.7 | 298. | IMRE | McMahon and Ohanessian, 2000 | Anchor alanine=39.89; RCD |
By formula: C9H13N+ + C6H6 = (C9H13N+ • C6H6)
Bond type: Charge transfer bond (positive ion)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 46.9 | kJ/mol | PHPMS | Meot-Ner (Mautner) and El-Shall, 1986 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 110. | J/mol*K | N/A | Meot-Ner (Mautner) and El-Shall, 1986 | gas phase; Entropy change calculated or estimated; M |
Free energy of reaction
ΔrG° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
11. | 331. | PHPMS | Meot-Ner (Mautner) and El-Shall, 1986 | gas phase; Entropy change calculated or estimated; M |
By formula: C7H9N+ + C6H6 = (C7H9N+ • C6H6)
Bond type: Charge transfer bond (positive ion)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 51.5 | kJ/mol | PHPMS | Meot-Ner (Mautner) and El-Shall, 1986 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 110. | J/mol*K | N/A | Meot-Ner (Mautner) and El-Shall, 1986 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 19. | kJ/mol | PHPMS | Meot-Ner (Mautner) and El-Shall, 1986 | gas phase; Entropy change calculated or estimated; M |
By formula: C8H11N+ + C6H6 = (C8H11N+ • C6H6)
Bond type: Charge transfer bond (positive ion)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 41.8 | kJ/mol | PHPMS | Meot-Ner (Mautner) and El-Shall, 1986 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 110. | J/mol*K | N/A | Meot-Ner (Mautner) and El-Shall, 1986 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 9.2 | kJ/mol | PHPMS | Meot-Ner (Mautner) and El-Shall, 1986 | gas phase; Entropy change calculated or estimated; M |
By formula: C10H10Fe+ + C6H6 = (C10H10Fe+ • C6H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 30. | kJ/mol | PHPMS | Meot-Ner (Mautner), 1989 | gas phase; Entropy change calculated or estimated, ΔrH<, DG<; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 84. | J/mol*K | N/A | Meot-Ner (Mautner), 1989 | gas phase; Entropy change calculated or estimated, ΔrH<, DG<; M |
Free energy of reaction
ΔrG° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
13. | 252. | PHPMS | Meot-Ner (Mautner), 1989 | gas phase; Entropy change calculated or estimated, ΔrH<, DG<; M |
By formula: (Co+ • C6H6) + C6H6 = (Co+ • 2C6H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 167. ± 14. | kJ/mol | CIDT | Meyer, Khan, et al., 1995 | RCD |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 116. | J/mol*K | SIDT | Kemper, Bushnell, et al., 1993 | gas phase; ΔrS(490 K); M |
Enthalpy of reaction
ΔrH° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
167. (+13.,-0.) | CID | Meyer, Khan, et al., 1995 | gas phase; guided ion beam CID; M | |
113. (+4.2,-0.) | SIDT | Kemper, Bushnell, et al., 1993 | gas phase; ΔrS(490 K); M |
By formula: C7H8+ + C6H6 = (C7H8+ • C6H6)
Bond type: Charge transfer bond (positive ion)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 51.0 | kJ/mol | MPI | Ernstberger, Krause, et al., 1990 | gas phase; M |
ΔrH° | 23. | kJ/mol | PI | Ruhl, Bisling, et al., 1986 | gas phase; from vIP of perpendicular dimer; M |
ΔrH° | 51.9 | kJ/mol | PHPMS | Meot-Ner (Mautner), Hamlet, et al., 1978 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 110. | J/mol*K | PHPMS | Meot-Ner (Mautner), Hamlet, et al., 1978 | gas phase; M |
By formula: C2H7O+ + C6H6 = (C2H7O+ • C6H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 88. | kJ/mol | PHPMS | Deakyne and Meot-Ner (Mautner), 1985 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 100. | J/mol*K | N/A | Deakyne and Meot-Ner (Mautner), 1985 | gas phase; Entropy change calculated or estimated; M |
Free energy of reaction
ΔrG° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
36. | 491. | PHPMS | Deakyne and Meot-Ner (Mautner), 1985 | gas phase; Entropy change calculated or estimated; M |
By formula: (K+ • C6H6 • H2O) + C6H6 = (K+ • 2C6H6 • H2O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 60.2 | kJ/mol | HPMS | Sunner, Nishizawa, et al., 1981 | gas phase; From thermochemical cycle,switching reaction(K+ 3H2O)C6H6, Searles and Kebarle, 1969; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 126. | J/mol*K | HPMS | Sunner, Nishizawa, et al., 1981 | gas phase; From thermochemical cycle,switching reaction(K+ 3H2O)C6H6, Searles and Kebarle, 1969; M |
By formula: (K+ • 2H2O • C6H6) + H2O = (K+ • 3H2O • C6H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 49.4 | kJ/mol | HPMS | Sunner, Nishizawa, et al., 1981 | gas phase; From thermochemical cycle,switching reaction(K+)4H2O; Searles and Kebarle, 1969; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 110. | J/mol*K | HPMS | Sunner, Nishizawa, et al., 1981 | gas phase; From thermochemical cycle,switching reaction(K+)4H2O; Searles and Kebarle, 1969; M |
By formula: (K+ • H2O • C6H6) + H2O = (K+ • 2H2O • C6H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 53.1 | kJ/mol | HPMS | Sunner, Nishizawa, et al., 1981 | gas phase; From thermochemical cycle,switching reaction(K+)3H2O; Searles and Kebarle, 1969; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 89.5 | J/mol*K | HPMS | Sunner, Nishizawa, et al., 1981 | gas phase; From thermochemical cycle,switching reaction(K+)3H2O; Searles and Kebarle, 1969; M |
By formula: I- + C6H6 = (I- • C6H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 26. ± 8.4 | kJ/mol | TDAs | Hiraoka, Mizuse, et al., 1988 | gas phase; B,M |
ΔrH° | 38. ± 4.2 | kJ/mol | TDAs | Caldwell, Masucci, et al., 1989 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 59.4 | J/mol*K | PHPMS | Hiraoka, Mizuse, et al., 1988 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 8. ± 11. | kJ/mol | TDAs | Hiraoka, Mizuse, et al., 1988 | gas phase; B |
By formula: C3H3+ + C6H6 = (C3H3+ • C6H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 38. | kJ/mol | HPMS | Field, Hamlet, et al., 1969 | gas phase; Entropy change is questionable; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 40. | J/mol*K | HPMS | Field, Hamlet, et al., 1969 | gas phase; Entropy change is questionable; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 30. | kJ/mol | HPMS | Field, Hamlet, et al., 1969 | gas phase; Entropy change is questionable; M |
By formula: (K+ • H2O • 2C6H6) + H2O = (K+ • 2H2O • 2C6H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 51.0 | kJ/mol | HPMS | Sunner, Nishizawa, et al., 1981 | gas phase; From thermochemical cycle(K+ 3H2O)C6H6; Searles and Kebarle, 1969; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 123. | J/mol*K | HPMS | Sunner, Nishizawa, et al., 1981 | gas phase; From thermochemical cycle(K+ 3H2O)C6H6; Searles and Kebarle, 1969; M |
By formula: (C6H6+ • 2C6H6) + C6H6 = (C6H6+ • 3C6H6)
Bond type: Charge transfer bond (positive ion)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 29. | kJ/mol | PHPMS | Hiraoka, Fujimaki, et al., 1991 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 84. | J/mol*K | N/A | Hiraoka, Fujimaki, et al., 1991 | gas phase; Entropy change calculated or estimated; M |
By formula: (K+ • C6H6 • 2H2O) + C6H6 = (K+ • 2C6H6 • 2H2O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 53.6 | kJ/mol | HPMS | Sunner, Nishizawa, et al., 1981 | gas phase; switching reaction(K+ 3H2O)C6H6; Searles and Kebarle, 1969; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 141. | J/mol*K | HPMS | Sunner, Nishizawa, et al., 1981 | gas phase; switching reaction(K+ 3H2O)C6H6; Searles and Kebarle, 1969; M |
By formula: Cr+ + C6H6 = (Cr+ • C6H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 168. | kJ/mol | MID | Lin, Chen, et al., 1997 | RCD |
ΔrH° | 164. ± 14. | kJ/mol | RAK | Lin and Dunbar, 1997 | RCD |
ΔrH° | 170. ± 10. | kJ/mol | CIDT | Meyer, Khan, et al., 1995 | RCD |
Enthalpy of reaction
ΔrH° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
170. (+9.6,-0.) | CID | Meyer, Khan, et al., 1995 | gas phase; guided ion beam CID; M |
By formula: (K+ • 2C6H6) + H2O = (K+ • H2O • 2C6H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 57.3 | kJ/mol | HPMS | Sunner, Nishizawa, et al., 1981 | gas phase; switching reaction(K+ 2H2O)C6H6; Searles and Kebarle, 1969; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 109. | J/mol*K | HPMS | Sunner, Nishizawa, et al., 1981 | gas phase; switching reaction(K+ 2H2O)C6H6; Searles and Kebarle, 1969; M |
By formula: (K+ • C6H6) + H2O = (K+ • H2O • C6H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 75.7 | kJ/mol | HPMS | Sunner, Nishizawa, et al., 1981 | gas phase; switching reaction(K+ C6H6)C6H6; Searles and Kebarle, 1969; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 125. | J/mol*K | HPMS | Sunner, Nishizawa, et al., 1981 | gas phase; switching reaction(K+ C6H6)C6H6; Searles and Kebarle, 1969; M |
By formula: (K+ • 2H2O) + C6H6 = (K+ • C6H6 • 2H2O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 56.1 | kJ/mol | HPMS | Sunner, Nishizawa, et al., 1981 | gas phase; switching reaction(K+)3H2O; Searles and Kebarle, 1969; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 102. | J/mol*K | HPMS | Sunner, Nishizawa, et al., 1981 | gas phase; switching reaction(K+)3H2O; Searles and Kebarle, 1969; M |
By formula: (K+ • 3H2O) + C6H6 = (K+ • C6H6 • 3H2O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 52.7 | kJ/mol | HPMS | Sunner, Nishizawa, et al., 1981 | gas phase; switching reaction(K+)4H2O; Searles and Kebarle, 1969; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 115. | J/mol*K | HPMS | Sunner, Nishizawa, et al., 1981 | gas phase; switching reaction(K+)4H2O; Searles and Kebarle, 1969; M |
By formula: (K+ • H2O) + C6H6 = (K+ • C6H6 • H2O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 70.3 | kJ/mol | HPMS | Sunner, Nishizawa, et al., 1981 | gas phase; switching reaction(K+)2H2O; Searles and Kebarle, 1969; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 113. | J/mol*K | HPMS | Sunner, Nishizawa, et al., 1981 | gas phase; switching reaction(K+)2H2O; Searles and Kebarle, 1969; M |
By formula: (Cr+ • C6H6) + C6H6 = (Cr+ • 2C6H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 212. ± 38. | kJ/mol | RAK | Lin and Dunbar, 1997 | RCD |
ΔrH° | 232. ± 18. | kJ/mol | CIDT | Meyer, Khan, et al., 1995 | RCD |
Enthalpy of reaction
ΔrH° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
231. (+18.,-0.) | CID | Meyer, Khan, et al., 1995 | gas phase; guided ion beam CID; M |
By formula: F- + C6H6 = (F- • C6H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 64.02 | kJ/mol | TDAs | Hiraoka, Mizuse, et al., 1987 | gas phase; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 81.6 | J/mol*K | PHPMS | Hiraoka, Mizuse, et al., 1987 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 39.3 | kJ/mol | TDAs | Hiraoka, Mizuse, et al., 1987 | gas phase; B |
By formula: Mn+ + C6H6 = (Mn+ • C6H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 144. | kJ/mol | MID | Lin, Chen, et al., 1997 | RCD |
ΔrH° | 133. ± 9.2 | kJ/mol | CIDT | Meyer, Khan, et al., 1995 | RCD |
Enthalpy of reaction
ΔrH° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
133. (+8.8,-0.) | CID | Meyer, Khan, et al., 1995 | gas phase; guided ion beam CID; M |
By formula: V+ + C6H6 = (V+ • C6H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | >230. | kJ/mol | RAK | Gapeev and Dunbar, 2002 | RCD |
ΔrH° | 234. ± 10. | kJ/mol | CIDT | Meyer, Khan, et al., 1995 | RCD |
Enthalpy of reaction
ΔrH° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
233. (+9.6,-0.) | CID | Meyer, Khan, et al., 1995 | gas phase; guided ion beam CID; M |
By formula: Fe+ + C6H6 = (Fe+ • C6H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 197. | kJ/mol | RAK | Gapeev and Dunbar, 2002 | RCD |
ΔrH° | 207. ± 12. | kJ/mol | CIDT | Meyer, Khan, et al., 1995 | RCD |
Enthalpy of reaction
ΔrH° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
208. (+9.6,-0.) | CID | Meyer, Khan, et al., 1995 | gas phase; guided ion beam CID; M |
By formula: Ti+ + C6H6 = (Ti+ • C6H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 213. | kJ/mol | RAK | Gapeev and Dunbar, 2002 | RCD |
ΔrH° | 259. ± 9.2 | kJ/mol | CIDT | Meyer, Khan, et al., 1995 | RCD |
Enthalpy of reaction
ΔrH° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
259. (+8.8,-0.) | CID | Meyer, Khan, et al., 1995 | gas phase; guided ion beam CID; M |
By formula: (K+ • C6H6) + C6H6 = (K+ • 2C6H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 67.4 ± 7.1 | kJ/mol | CIDT | Amicangelo and Armentrout, 2000 | RCD |
ΔrH° | 78.7 | kJ/mol | HPMS | Sunner, Nishizawa, et al., 1981 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 142. | J/mol*K | HPMS | Sunner, Nishizawa, et al., 1981 | gas phase; M |
By formula: C4H9+ + C6H6 = (C4H9+ • C6H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 92. | kJ/mol | PHPMS | Sen Sharma, Ikuta, et al., 1982 | gas phase; forms protonated t-butylbenzene; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 210. | J/mol*K | PHPMS | Sen Sharma, Ikuta, et al., 1982 | gas phase; forms protonated t-butylbenzene; M |
By formula: (C6H6+ • C6H6) + C6H6 = (C6H6+ • 2C6H6)
Bond type: Charge transfer bond (positive ion)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 33. ± 2. | kJ/mol | PHPMS | Hiraoka, Fujimaki, et al., 1991 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 82.8 | J/mol*K | PHPMS | Hiraoka, Fujimaki, et al., 1991 | gas phase; M |
By formula: K+ + C6H6 = (K+ • C6H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 73. ± 4. | kJ/mol | CIDT | Amicangelo and Armentrout, 2000 | RCD |
ΔrH° | 80.3 | kJ/mol | HPMS | Sunner, Nishizawa, et al., 1981 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 103. | J/mol*K | HPMS | Sunner, Nishizawa, et al., 1981 | gas phase; M |
By formula: C6H7N+ + C6H6 = (C6H7N+ • C6H6)
Bond type: Charge transfer bond (positive ion)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 49.8 | kJ/mol | PHPMS | Meot-Ner (Mautner) and El-Shall, 1986 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 94.6 | J/mol*K | PHPMS | Meot-Ner (Mautner) and El-Shall, 1986 | gas phase; M |
By formula: C11H10+ + C6H6 = (C11H10+ • C6H6)
Bond type: Charge transfer bond (positive ion)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 38. | kJ/mol | PHPMS | El-Shall and Meot-Ner (Mautner), 1987 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 100. | J/mol*K | PHPMS | El-Shall and Meot-Ner (Mautner), 1987 | gas phase; M |
By formula: C6H5Cl+ + C6H6 = (C6H5Cl+ • C6H6)
Bond type: Charge transfer bond (positive ion)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 58.6 | kJ/mol | PHPMS | Meot-Ner (Mautner), Hamlet, et al., 1978 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 110. | J/mol*K | PHPMS | Meot-Ner (Mautner), Hamlet, et al., 1978 | gas phase; M |
By formula: C9H12+ + C6H6 = (C9H12+ • C6H6)
Bond type: Charge transfer bond (positive ion)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 44.4 | kJ/mol | PHPMS | Meot-Ner (Mautner), Hamlet, et al., 1978 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 110. | J/mol*K | PHPMS | Meot-Ner (Mautner), Hamlet, et al., 1978 | gas phase; M |
By formula: NO- + C6H6 = (NO- • C6H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 172. | kJ/mol | ICR | Reents and Freiser, 1981 | gas phase; switching reaction,Thermochemical ladder(NO+)C2H5OH, Entropy change calculated or estimated; Farid and McMahon, 1978; M |
By formula: (Fe+ • C6H6) + C6H6 = (Fe+ • 2C6H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 187. ± 16. | kJ/mol | CIDT | Meyer, Khan, et al., 1995 | RCD |
Enthalpy of reaction
ΔrH° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
187. (+16.,-0.) | CID | Meyer, Khan, et al., 1995 | gas phase; guided ion beam CID; M |
By formula: (Ti+ • C6H6) + C6H6 = (Ti+ • 2C6H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 253. ± 18. | kJ/mol | CIDT | Meyer, Khan, et al., 1995 | RCD |
Enthalpy of reaction
ΔrH° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
253. (+18.,-0.) | CID | Meyer, Khan, et al., 1995 | gas phase; guided ion beam CID; M |
By formula: (Mn+ • C6H6) + C6H6 = (Mn+ • 2C6H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 203. ± 16. | kJ/mol | CIDT | Meyer, Khan, et al., 1995 | RCD |
Enthalpy of reaction
ΔrH° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
203. (+16.,-0.) | CID | Meyer, Khan, et al., 1995 | gas phase; guided ion beam CID; M |
By formula: (Ni+ • C6H6) + C6H6 = (Ni+ • 2C6H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 147. ± 12. | kJ/mol | CIDT | Meyer, Khan, et al., 1995 | RCD |
Enthalpy of reaction
ΔrH° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
147. (+12.,-0.) | CID | Meyer, Khan, et al., 1995 | gas phase; guided ion beam CID; M |
By formula: (Cu+ • C6H6) + C6H6 = (Cu+ • 2C6H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 155. ± 12. | kJ/mol | CIDT | Meyer, Khan, et al., 1995 | RCD |
Enthalpy of reaction
ΔrH° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
155. (+12.,-0.) | CID | Meyer, Khan, et al., 1995 | gas phase; guided ion beam CID; M |
(CAS Reg. No. 79431-04-2 • 4294967295) + = CAS Reg. No. 79431-04-2
By formula: (CAS Reg. No. 79431-04-2 • 4294967295C6H6) + C6H6 = CAS Reg. No. 79431-04-2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 90. ± 18. | kJ/mol | Ther | Lee and Squires, 1986 | gas phase; Between SiH4, tBuOH; value altered from reference due to change in acidity scale; B |
By formula: Ni+ + C6H6 = (Ni+ • C6H6)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 243. ± 11. | kJ/mol | CIDT | Meyer, Khan, et al., 1995 | RCD |
Enthalpy of reaction
ΔrH° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
243. (+10.,-0.) | CID | Meyer, Khan, et al., 1995 | gas phase; guided ion beam CID; M |
Henry's Law data
Go To: Top, Gas 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 |
---|---|---|---|---|
0.18 | M | N/A | missing citation also measured solubilities in salt solutions. | |
0.16 | 4100. | L | N/A | |
0.21 | 3600. | M | N/A | |
0.21 | M | N/A | ||
0.18 | X | N/A | Value given here as cited in missing citation. | |
0.17 | M | N/A | ||
0.19 | 3800. | M | N/A | |
0.17 | 3900. | X | N/A | |
0.18 | Q | N/A | missing citation give several references for the Henry's law constants but don't assign them to specific species. | |
0.16 | 4300. | X | N/A | |
0.18 | 3200. | X | N/A | |
0.18 | 2200. | X | N/A | |
0.18 | 4000. | X | Leighton and Calo, 1981 | |
0.18 | L | N/A | ||
0.12 | 5300. | X | N/A | |
0.19 | 4300. | X | N/A | |
0.18 | M | Mackay, Shiu, et al., 1979 | ||
0.18 | T | Mackay, Shiu, et al., 1979 | ||
0.18 | V | N/A | ||
0.18 | M | N/A | ||
0.22 | 4200. | M | N/A | |
0.16 | 4500. | M | N/A | |
0.18 | V | Bohon and Claussen, 1951 |
References
Go To: Top, Gas 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.
Roux, Temprado, et al., 2008
Roux, M.V.; Temprado, M.; Chickos, J.S.; Nagano, Y.,
Critically Evaluated Thermochemical Properties of Polycyclic Aromatic Hydrocarbons,
J. Phys. Chem. Ref. Data, 2008, 37, 4, 1855-1996. [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]
Prosen, Gilmont, et al., 1945
Prosen, E.J.; Gilmont, R.; Rossini, F.D.,
Heats of combustion of benzene, toluene, ethyl-benzene, o-xylene, m-xylene, p-xylene, n-propylbenzene, and styrene,
J. Res. NBS, 1945, 34, 65-70. [all data]
Prosen, Johnson, et al., 1946
Prosen, E.J.; Johnson, W.H.; Rossini, F.D.,
Heats of combustion and formation at 25°C of the alkylbenzenes through C10H14, and of the higher normal monoalkylbenzenes,
J. Res. NBS, 1946, 36, 455-461. [all data]
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Gas-Phase Binding Energies and Spectroscopic Properties of NO+ Charge-Transfer Complexes,
J. Am. Chem. Soc., 1981, 103, 2791. [all data]
Farid and McMahon, 1978
Farid, R.; McMahon, T.B.,
Gas-Phase Ion-Molecule Reactions of Alkyl Nitrites by Ion Cyclotron Resonance Spectroscopy,
Int. J. Mass Spectrom. Ion Phys., 1978, 27, 2, 163, https://doi.org/10.1016/0020-7381(78)80037-0
. [all data]
Lee and Squires, 1986
Lee, R.E.; Squires, R.R.,
Anionic homoaromaticity: A gas phase experimental study,
J. Am. Chem. Soc., 1986, 105, 5078. [all data]
Leighton and Calo, 1981
Leighton, D.T.; Calo, J.M.,
Distribution Coefficients of Chlorinated Hydrocarbons in Dilute Air-Water Systems for Groundwater Contamination Applications,
J. Chem. Eng. Data, 1981, 26, 382-385. [all data]
Mackay, Shiu, et al., 1979
Mackay, D.; Shiu, W.-Y.; Sutherland, R.P.,
Determination of Air-Water Henry's Law Constants for Hydrophobic Pollutants,
Environ. Sci. Technol., 1979, 13, 333-337. [all data]
Bohon and Claussen, 1951
Bohon, R.L.; Claussen, W.F.,
The solubility of aromatic hydrocarbons in water,
J. Am. Chem. Soc., 1951, 73, 1571-1578. [all data]
Notes
Go To: Top, Gas phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, References
- Symbols used in this document:
Cp,gas Constant pressure heat capacity of gas Pc Critical pressure T Temperature Tboil Boiling point Tc Critical temperature Tfus Fusion (melting) point 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 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 ΔrS° Entropy of reaction at standard conditions ΔsubH Enthalpy of sublimation ΔsubH° Enthalpy of sublimation 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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