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, Henry's Law data, Gas phase ion energetics 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 | 19.8 ± 0.2 | kcal/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 | 19.8 | kcal/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 | 19.82 ± 0.12 | kcal/mol | Ccb | Prosen, Gilmont, et al., 1945 | Hf by Prosen, Johnson, et al., 1946; ALS |
ΔfH°gas | 19.1 | kcal/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 (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
7.952 | 50. | Thermodynamics Research Center, 1997 | GT |
8.391 | 100. | ||
10.02 | 150. | ||
12.71 | 200. | ||
17.82 | 273.15 | ||
19.70 | 298.15 | ||
19.84 | 300. | ||
27.132 | 400. | ||
33.305 | 500. | ||
38.262 | 600. | ||
42.251 | 700. | ||
45.519 | 800. | ||
48.236 | 900. | ||
50.528 | 1000. | ||
52.476 | 1100. | ||
54.140 | 1200. | ||
55.566 | 1300. | ||
56.800 | 1400. | ||
57.866 | 1500. | ||
59.969 | 1750. | ||
61.487 | 2000. | ||
62.608 | 2250. | ||
63.456 | 2500. | ||
64.109 | 2750. | ||
64.620 | 3000. |
Constant pressure heat capacity of gas
Cp,gas (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
22.30 ± 0.01 | 333.15 | Todd S.S., 1978 | Please also see Montgomery J.B., 1942, Pitzer K.S., 1943, Scott D.W., 1947.; GT |
22.90 | 341.60 | ||
23.42 ± 0.01 | 348.15 | ||
24.85 ± 0.01 | 368.15 | ||
25.100 | 370. | ||
25.041 | 371.20 | ||
26.00 ± 0.30 | 388. | ||
26.501 | 390. | ||
26.40 ± 0.30 | 393. | ||
27.230 | 402.30 | ||
27.32 ± 0.02 | 403.15 | ||
27.600 | 410. | ||
28.10 ± 0.30 | 417. | ||
28.40 ± 0.30 | 428. | ||
29.491 | 436.15 | ||
29.62 ± 0.02 | 438.15 | ||
30.30 ± 0.30 | 463. | ||
31.649 | 471.10 | ||
31.77 ± 0.02 | 473.15 | ||
31.40 ± 0.30 | 481. | ||
33.33 ± 0.02 | 500.15 | ||
34.80 ± 0.02 | 527.15 |
Phase change data
Go To: Top, Gas phase thermochemistry data, Henry's Law data, Gas phase ion energetics 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 | 48.3 ± 0.4 | atm | 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° | 8.10 ± 0.03 | kcal/mol | AVG | N/A | Average of 10 out of 11 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ΔsubH° | 10.6 | kcal/mol | TE,ME | Kruif, 1980 | Based on data from 183. to 197. K.; AC |
Enthalpy of vaporization
ΔvapH (kcal/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
7.342 | 353.3 | N/A | Majer and Svoboda, 1985 | |
7.93 | 320. | N/A | Lubomska, Banas, et al., 2002 | Based on data from 305. to 345. K.; AC |
8.51 | 258. to 313. | GC | Liu and Dickhut, 1994 | AC |
8.01 | 311. | EB | Ambrose, Ewing, et al., 1990 | Based on data from 296. to 377. K.; AC |
7.98 | 307. | C | Dong, Lin, et al., 1988 | AC |
7.91 | 314. | C | Dong, Lin, et al., 1988 | AC |
7.74 | 324. | C | Dong, Lin, et al., 1988 | AC |
7.62 | 332. | C | Dong, Lin, et al., 1988 | AC |
7.50 | 344. | C | Dong, Lin, et al., 1988 | AC |
7.31 | 353. | C | Dong, Lin, et al., 1988 | AC |
8.22 | 294. | A | Stephenson and Malanowski, 1987 | Based on data from 279. to 377. K.; AC |
7.53 | 368. | A | Stephenson and Malanowski, 1987 | Based on data from 353. to 422. K.; AC |
7.22 | 435. | A | Stephenson and Malanowski, 1987 | Based on data from 420. to 502. K.; AC |
7.24 | 516. | A | Stephenson and Malanowski, 1987 | Based on data from 501. to 562. K.; AC |
7.36 | 352. | N/A | Natarajan, 1983 | AC |
7.29 | 361. | N/A | Natarajan, 1983 | AC |
7.22 | 366. | N/A | Natarajan, 1983 | AC |
8.44 | 343. | N/A | Tsonopoulos and Wilson, 1983 | Based on data from 313. to 373. K.; AC |
7.4 | 350. | N/A | Rao and Viswanath, 1977 | AC |
7.89 ± 0.02 | 313. | C | Svoboda, Veselý, et al., 1973 | AC |
7.70 ± 0.02 | 328. | C | Svoboda, Veselý, et al., 1973 | AC |
7.60 ± 0.02 | 333. | C | Svoboda, Veselý, et al., 1973 | AC |
7.50 ± 0.02 | 343. | C | Svoboda, Veselý, et al., 1973 | AC |
7.39 ± 0.02 | 353. | C | Svoboda, Veselý, et al., 1973 | AC |
7.79 ± 0.1 | 313. | DSC | Mita, Imai, et al., 1971 | AC |
7.8 ± 0.1 | 328. | DSC | Mita, Imai, et al., 1971 | AC |
7.55 ± 0.1 | 345. | DSC | Mita, Imai, et al., 1971 | AC |
8.15 | 299. | N/A | Forziati, Norris, et al., 1949 | Based on data from 284. to 354. K.; AC |
8.15 | 293. | N/A | Yarym-Agaev, Fedos'ev, et al., 1949 | AC |
8.15 | 297. | N/A | Thomson, 1946 | Based on data from 282. to 354. K.; AC |
7.46 | 294. | N/A | Scott and Brickwedde, 1945 | AC |
8.15 | 303. | MM | Willingham, Taylor, et al., 1945 | Based on data from 288. to 354. K.; AC |
7.98 | 313. | EB | Smith, 1941 | Based on data from 298. to 373. K.; AC |
8.25 | 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)
(kcal/mol)
Tr = reduced temperature (T / Tc)
View plot Requires a JavaScript / HTML 5 canvas capable browser.
Temperature (K) | 293. to 469. |
---|---|
A (kcal/mol) | 11.33 |
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 (atm)
T = temperature (K)
View plot Requires a JavaScript / HTML 5 canvas capable browser.
Temperature (K) | A | B | C | Reference | Comment |
---|---|---|---|---|---|
333.4 to 373.5 | 4.72012 | 1660.652 | -1.461 | Eon, Pommier, et al., 1971 | Coefficents calculated by NIST from author's data. |
297.9 to 318. | 0.14020 | 39.165 | -261.236 | Deshpande and Pandya, 1967 | Coefficents calculated by NIST from author's data. |
421.56 to 554.8 | 4.59791 | 1701.073 | 20.806 | Kalafati, Rasskazov, et al., 1967 | Coefficents calculated by NIST from author's data. |
287.70 to 354.07 | 4.01243 | 1203.835 | -53.226 | Williamham, Taylor, et al., 1945 |
Enthalpy of sublimation
ΔsubH (kcal/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
9.97 | 258. to 273. | N/A | Liu and Dickhut, 1994 | AC |
10.8 | 264. | A | Stephenson and Malanowski, 1987 | Based on data from 223. to 279. K. See also Ha, Morrison, et al., 1976.; AC |
10.8 | 278. | N/A | Hessler, 1984 | AC |
12.9 ± 0.2 | 193. | N/A | De Kruif and Van Ginkel, 1977 | AC |
11.8 ± 0.1 | 193. | N/A | De Kruif and Van Ginkel, 1977 | AC |
10.9 | 279. | MM | Jackowski, 1974 | Based on data from 221. to 268. K.; AC |
10.5 | 261. | N/A | Jones, 1960 | AC |
10.3 | 229. | N/A | Jones, 1960 | AC |
10.7 | 279. | N/A | Milazzo, 1956 | AC |
11.1 | 282. | A | Stull, 1947 | Based on data from 263. to 270. K.; AC |
9.2 | 303. | V | Wolf and Weghofer, 1938 | ALS |
10.7 | 273. | N/A | de Boer, 1936 | See also Jackowski, 1974.; AC |
10.3 | 226. | A | Mündel, 1913 | Based on data from 214. to 238. K.; AC |
Enthalpy of fusion
ΔfusH (kcal/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
2.3581 | 278.69 | N/A | Oliver, Eaton, et al., 1948 | DH |
2.370 | 278.65 | N/A | Ziegler and Andrews, 1942 | DH |
2.36 | 278.7 | C | Domalski and Hearing, 1996 | See also Andrews, Lynn, et al., 1926 and Ziegler and Andrews, 1942.; AC |
2.223 | 279.1 | N/A | Smith, 1979 | DH |
2.139 | 278.8 | N/A | Pacor, 1967 | DH |
2.375 | 278.6 | N/A | Tschamler, 1948 | DH |
2.343 | 278.6 | N/A | Huffman, Parks, et al., 1930 | DH |
2.360 | 278.55 | N/A | Andrews, Lynn, et al., 1926 | DH |
2.3901 | 278.64 | N/A | Maass and Walbauer, 1925 | DH |
Entropy of fusion
ΔfusS (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
8.461 | 278.69 | Oliver, Eaton, et al., 1948 | DH |
8.506 | 278.65 | Ziegler and Andrews, 1942 | DH |
7.96 | 279.1 | Smith, 1979 | DH |
7.67 | 278.8 | Pacor, 1967 | DH |
8.411 | 278.6 | Huffman, Parks, et al., 1930 | DH |
8.48 | 278.55 | Andrews, Lynn, et al., 1926 | DH |
8.58 | 278.64 | Maass and Walbauer, 1925 | DH |
Henry's Law data
Go To: Top, Gas phase thermochemistry data, Phase change data, Gas phase ion energetics 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 |
Gas phase ion energetics 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 evaluated as indicated in comments:
HL - Edward P. Hunter and Sharon G. Lias
L - Sharon G. Lias
Data compiled as indicated in comments:
B - John E. Bartmess
MM - Michael M. Meot-Ner (Mautner)
LL - Sharon G. Lias and Joel F. Liebman
LBLHLM - Sharon G. Lias, John E. Bartmess, Joel F. Liebman, John L. Holmes, Rhoda D. Levin, and W. Gary Mallard
LLK - Sharon G. Lias, Rhoda D. Levin, and Sherif A. Kafafi
RDSH - Henry M. Rosenstock, Keith Draxl, Bruce W. Steiner, and John T. Herron
View reactions leading to C6H6+ (ion structure unspecified)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
IE (evaluated) | 9.24378 ± 0.00007 | eV | N/A | N/A | L |
Quantity | Value | Units | Method | Reference | Comment |
Proton affinity (review) | 179.3 | kcal/mol | N/A | Hunter and Lias, 1998 | HL |
Quantity | Value | Units | Method | Reference | Comment |
Gas basicity | 173.4 | kcal/mol | N/A | Hunter and Lias, 1998 | HL |
Proton affinity at 298K
Proton affinity (kcal/mol) | Reference | Comment |
---|---|---|
178.4 | Aue, Guidoni, et al., 2000 | Experimental literature data re-evaluated by the authors using ab initio protonation entropies; MM |
Gas basicity at 298K
Gas basicity (review) (kcal/mol) | Reference | Comment |
---|---|---|
172.5 | Aue, Guidoni, et al., 2000 | Experimental literature data re-evaluated by the authors using ab initio protonation entropies; MM |
Ionization energy determinations
Appearance energy determinations
De-protonation reactions
C6H5- + =
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 401.22 ± 0.50 | kcal/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° | 401.16 ± 0.21 | kcal/mol | D-EA | Gunion, Gilles, et al., 1992 | gas phase; B |
ΔrH° | 400.7 ± 2.5 | kcal/mol | TDEq | Meot-ner and Sieck, 1986 | gas phase; B |
ΔrH° | 401. ± 10. | kcal/mol | CIDT | Graul and Squires, 1990 | gas phase; B |
ΔrH° | 398.0 ± 5.6 | kcal/mol | G+TS | Bohme and Young, 1971 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 392.40 ± 0.40 | kcal/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° | 390.9 ± 2.0 | kcal/mol | TDEq | Meot-ner and Sieck, 1986 | gas phase; B |
ΔrG° | 390.1 ± 6.5 | kcal/mol | IMRB | Bartmess and McIver Jr., 1979 | gas phase; B |
ΔrG° | 389.2 ± 5.5 | kcal/mol | IMRB | Bohme and Young, 1971 | gas phase; B |
References
Go To: Top, Gas phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics 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]
Landrieu, Baylocq, et al., 1929
Landrieu, P.; Baylocq, F.; Johnson, J.R.,
Etude thermochimique dans la serie furanique,
Bull. Soc. Chim. France, 1929, 45, 36-49. [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]
Todd S.S., 1978
Todd S.S.,
Vapor-flow calorimetry of benzene,
J. Chem. Thermodyn., 1978, 10, 641-648. [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]
Pitzer K.S., 1943
Pitzer K.S.,
The thermodynamics and molecular structure of benzene and its methyl derivatives,
J. Am. Chem. Soc., 1943, 65, 803-829. [all data]
Scott D.W., 1947
Scott D.W.,
The heat capacity of benzene vapor. The contribution of anharmonicity,
J. Chem. Phys., 1947, 15, 565-568. [all data]
Kruif, 1980
Kruif, C.G.,
Enthalpies of sublimation and vapour pressures of 11 polycyclic hydrocarbons,
J. Chem. Thermodyn., 1980, 12, 243-248. [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]
Lubomska, Banas, et al., 2002
Lubomska, Monika; Banas, Agnieszka; Malanowski, Stanislaw K.,
Vapor-Liquid Equilibrium in Binary Systems Formed by Allyl Alcohol with Benzene and with Cyclohexane,
J. Chem. Eng. Data, 2002, 47, 6, 1466-1471, https://doi.org/10.1021/je025540l
. [all data]
Liu and Dickhut, 1994
Liu, Kewen; Dickhut, Rebecca M.,
Saturation vapor pressures and thermodynamic properties of benzene and selected chlorinated benzenes at environmental temperatures,
Chemosphere, 1994, 29, 3, 581-589, https://doi.org/10.1016/0045-6535(94)90445-6
. [all data]
Ambrose, Ewing, et al., 1990
Ambrose, D.; Ewing, M.B.; Ghiassee, N.B.; Sanchez Ochoa, J.C.,
The ebulliometric method of vapour-pressure measurement: vapour pressures of benzene, hexafluorobenzene, and naphthalene,
The Journal of Chemical Thermodynamics, 1990, 22, 6, 589-605, https://doi.org/10.1016/0021-9614(90)90151-F
. [all data]
Dong, Lin, et al., 1988
Dong, Jin-Quan; Lin, Rui-Sen; Yen, Wen-Hsing,
Heats of vaporization and gaseous molar heat capacities of ethanol and the binary mixture of ethanol and benzene,
Can. J. Chem., 1988, 66, 4, 783-790, https://doi.org/10.1139/v88-136
. [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]
Natarajan, 1983
Natarajan, G.,
High-temperature calorimeter for the measurement of vapor pressure and enthalpy of vaporization,
Rev. Sci. Instrum., 1983, 54, 9, 1175, https://doi.org/10.1063/1.1137545
. [all data]
Tsonopoulos and Wilson, 1983
Tsonopoulos, Constantine; Wilson, G.M.,
High-temperature mutual solubilities of hydrocarbons and water. Part I: Benzene, cyclohexane andn-hexane,
AIChE J., 1983, 29, 6, 990-999, https://doi.org/10.1002/aic.690290618
. [all data]
Rao and Viswanath, 1977
Rao, Yaddanapudi J.; Viswanath, Dabir S.,
Integral isobaric heats of vaporization of benzene-chloroethane systems,
J. Chem. Eng. Data, 1977, 22, 1, 36-38, https://doi.org/10.1021/je60072a011
. [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]
Mita, Imai, et al., 1971
Mita, Itaru; Imai, Isao; Kambe, Hirotaro,
Determination of heat of mixing and heat of vaporization with a differential scanning calorimeter,
Thermochimica Acta, 1971, 2, 4, 337-344, https://doi.org/10.1016/0040-6031(71)85035-9
. [all data]
Forziati, Norris, et al., 1949
Forziati, Alphonse F.; Norris, William R.; Rossini, Frederick D.,
Vapor pressures and boiling points of sixty API-NBS hydrocarbons,
J. RES. NATL. BUR. STAN., 1949, 43, 6, 555-17, https://doi.org/10.6028/jres.043.050
. [all data]
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. [all data]
Gunion, Gilles, et al., 1992
Gunion, R.F.; Gilles, M.K.; Polak, M.L.; Lineberger, W.C.,
Ultraviolet Photoelectron Spectroscopy of the Phenide, Benzyl, and Phenoxide Anions.,
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. [all data]
Meot-ner and Sieck, 1986
Meot-ner, M.; Sieck, L.W.,
Relative acidities of water and methanol, and the stabilities of the dimer adducts,
J. Phys. Chem., 1986, 90, 6687. [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]
Bohme and Young, 1971
Bohme, D.K.; Young, L.B.,
Electron affinities from thermal proton transfer reactions: C6H5 and C6H5CH2,
Can. J. Chem., 1971, 49, 2918. [all data]
Bartmess and McIver Jr., 1979
Bartmess, J.E.; McIver Jr.,
The Gas Phase Acidity Scale
in Gas Phase Ion Chemistry, Gas Phase Ion Chemistry, V. 2, M.T. Bowers, Ed., Academic Press, NY, 1979, Ch. 11, Elsevier, 1979. [all data]
Notes
Go To: Top, Gas phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics data, References
- Symbols used in this document:
AE Appearance energy Cp,gas Constant pressure heat capacity of gas IE (evaluated) Recommended ionization energy Pc Critical pressure 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 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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