Toluene
- Formula: C7H8
- Molecular weight: 92.1384
- IUPAC Standard InChIKey: YXFVVABEGXRONW-UHFFFAOYSA-N
- CAS Registry Number: 108-88-3
- 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: Benzene, methyl; Methacide; Methylbenzene; Methylbenzol; Phenylmethane; Antisal 1a; Toluol; Methane, phenyl-; NCI-C07272; Tolueen; Toluen; Toluolo; Rcra waste number U220; Tolu-sol; UN 1294; Dracyl; Monomethyl benzene; CP 25; NSC 406333; methylbenzene (toluene)
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Gas phase thermochemistry data
Go To: Top, Condensed phase thermochemistry 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 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 | 50.1 ± 1.1 | 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 | 50.00 ± 0.63 | kJ/mol | Ccb | Prosen, Gilmont, et al., 1945 | Hf by Prosen, Johnson, et al., 1946; ALS |
ΔfH°gas | 48.0 | kJ/mol | N/A | Schmidlin, 1906 | Value computed using ΔfHliquid° value of 10.0 kj/mol from Schmidlin, 1906 and ΔvapH° value of 38.0 kj/mol from Prosen, Gilmont, et al., 1945.; DRB |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
69.85 | 200. | Draeger, 1985 | Recommended values agree better with experimental heat capacities than results of calculation [ Chao J., 1984]. All other statistically calculated values [ Pitzer K.S., 1943, Taylor W.J., 1946, Scott D.W., 1962] are in close agreement with selected ones, except for high temperatures.; GT |
94.68 | 273.15 | ||
103.7 ± 0.4 | 298.15 | ||
104.4 | 300. | ||
139.9 | 400. | ||
170.8 | 500. | ||
196.2 | 600. | ||
217.0 | 700. | ||
234.3 | 800. | ||
248.9 | 900. | ||
261.2 | 1000. | ||
271.8 | 1100. | ||
280.8 | 1200. | ||
288.5 | 1300. | ||
295.2 | 1400. | ||
301.0 | 1500. |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
130.08 ± 0.26 | 371.20 | Scott D.W., 1962 | Please also see Montgomery J.B., 1942, Pitzer K.S., 1943, Taylor W.J., 1946.; GT |
140.2 | 390. | ||
137.2 ± 1.3 | 393. | ||
138.87 ± 0.27 | 396.20 | ||
146.4 | 410. | ||
149.16 ± 0.30 | 427.20 | ||
149.4 ± 1.7 | 428. | ||
160.33 ± 0.32 | 462.20 | ||
159.0 ± 1.7 | 463. | ||
171.46 ± 0.34 | 500.20 |
Condensed phase thermochemistry data
Go To: Top, Gas phase thermochemistry 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 as indicated in comments:
DRB - Donald R. Burgess, Jr.
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 | 12. ± 1.1 | 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°liquid | 12.0 ± 0.63 | kJ/mol | Ccb | Prosen, Gilmont, et al., 1945 | Hf by Prosen, Johnson, et al., 1946; ALS |
ΔfH°liquid | Ccb | Schmidlin, 1906 | uncertain value: 10. kJ/mol; Undetermine error; ALS | ||
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -3920. ± 20. | kJ/mol | AVG | N/A | Average of 5 out of 6 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
S°liquid | 220.96 | J/mol*K | N/A | Scott, Guthrie, et al., 1962 | DH |
S°liquid | 219.2 | J/mol*K | N/A | Kelley, 1929 | DH |
Constant pressure heat capacity of liquid
Cp,liquid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
157.09 | 298.15 | Grolier, Roux-Desgranges, et al., 1993 | DH |
155.96 | 298.15 | Shiohama, Ogawa, et al., 1988 | DH |
159.9 | 303.15 | Reddy, 1986 | T = 303.15, 313.15 K.; DH |
157.08 | 298.15 | Roux-Dexgranges, Grolier, et al., 1986 | DH |
158.70 | 298.15 | Tardajos, Aicart, et al., 1986 | DH |
158.7 | 298.15 | Stephens and Olson, 1984 | T = 266 to 318 K. Cp given as 0.4117 cal g-1 C-1.; DH |
157.0 | 298.15 | Grolier, Inglese, et al., 1982 | DH |
157.15 | 298.15 | Wilhelm, Faradjzadeh, et al., 1982 | DH |
156.0 | 293.15 | Atalla, El-Sharkawy, et al., 1981 | DH |
157.0 | 294.71 | Andolenko and Grigor'ev, 1979 | T = 293 to 373 K. Unsoothed experimental datum given as 1.704 KJ/kg*K.; DH |
157.057 | 298.15 | Fortier and Benson, 1979 | DH |
157.081 | 298.15 | Fortier and Benson, 1977 | DH |
156.94 | 298.15 | Wilhelm, Grolier, et al., 1977 | DH |
157.026 | 298.15 | Fortier and Benson, 1976 | DH |
156.99 | 298.15 | Holzhauer and Ziegler, 1975 | T = 165 to 312 K. Cp = 187.43814 - 0.73026493T + 0.0029613602T2 - 2.8661704x10-6T3 J/mol*K.; DH |
158.4 | 298.15 | Pedersen, Kay, et al., 1975 | T = 298 to 348 K. Cp(liq) = 154.73 + 0.0981(T/K-273.15) + 0.001949(T/K-273.15)2 J/mol*K (298 to 348 K).; DH |
156.8 | 298.15 | Rajagopal and Subrahmanyam, 1974 | T = 298.15 to 323.15 K.; DH |
156.5 | 298. | Deshpande and Bhatagadde, 1971 | T = 298 to 318 K.; DH |
158.6 | 293. | Rastorguev and Ganiev, 1967 | T = 293 to 373 K.; DH |
157.33 | 298.711 | Hwa and Ziegler, 1966 | T = 181 to 304 K. Unsmoothed experimental datum.; DH |
157.23 | 298.15 | Scott, Guthrie, et al., 1962 | T = 10 to 360 K.; DH |
166.9 | 324. | Swietoslawski and Zielenkiewicz, 1958 | Mean value 21 to 81 C.; DH |
140. | 295. | Tschamler, 1948 | DH |
158.6 | 298. | Kurbatov, 1947 | T = -76 to 60 C, mean Cp, four temperatures.; DH |
156.9 | 298.1 | Zhdanov, 1941 | T = 5 to 47 C.; DH |
157.07 | 298.2 | Burlew, 1940 | T = 281 to 383 K.; DH |
156.5 | 298. | Vold, 1937 | DH |
142.7 | 227.8 | Aoyama and Kanda, 1935 | T = 78 to 228 K. Value is unsmoothed experimental datum.; DH |
156.5 | 298.1 | Richards and Wallace, 1932 | T = 293 to 333 K.; DH |
161.9 | 298.15 | Smith and Andrews, 1931 | T = 102 to 299 K. Value is unsmoothed experimental datum.; DH |
153.09 | 28.444 | Kelley, 1929 | T = 14 to 284 K. Value is unsmoothed experimental datum.; DH |
151.0 | 293.2 | Williams and Daniels, 1925 | T = 20 to 60 C.; DH |
153.6 | 303. | Willams and Daniels, 1924 | T = 303 to 343 K. Equation only.; DH |
158.2 | 298. | von Reis, 1881 | T = 292 to 390 K.; DH |
Reaction thermochemistry 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:
B - John E. Bartmess
M - Michael M. Meot-Ner (Mautner) and Sharon G. Lias
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
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.
Individual Reactions
C7H7- + =
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1599.7 ± 1.9 | kJ/mol | D-EA | Gunion, Gilles, et al., 1992 | gas phase; Kim, Wenthold, et al., 1999, with LN2 cooling of the ion, gives the same EA; B |
ΔrH° | 1593. ± 8.8 | kJ/mol | G+TS | Bartmess, Scott, et al., 1979 | gas phase; value altered from reference due to change in acidity scale; B |
ΔrH° | 1587. ± 8.8 | kJ/mol | G+TS | Gal, Decouzon, et al., 2001 | gas phase; B |
ΔrH° | 1577. ± 15. | kJ/mol | CIDT | Graul and Squires, 1990 | gas phase; B |
ΔrH° | 1609. ± 30. | kJ/mol | G+TS | Bohme and Young, 1971 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1564. ± 8.4 | kJ/mol | IMRE | Bartmess, Scott, et al., 1979 | gas phase; value altered from reference due to change in acidity scale; B |
ΔrG° | 1557. ± 8.4 | kJ/mol | IMRE | Gal, Decouzon, et al., 2001 | gas phase; B |
ΔrG° | 1579. ± 29. | kJ/mol | IMRB | Bohme and Young, 1971 | gas phase; B |
By formula: C3H9Si+ + C7H8 = (C3H9Si+ • C7H8)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 119. | kJ/mol | PHPMS | Stone and Stone, 1991 | gas phase; forms pi complex; M |
ΔrH° | 131. | kJ/mol | PHPMS | Stone and Stone, 1991 | gas phase; toluene D8, forms pi complex; M |
ΔrH° | 111. | kJ/mol | PHPMS | Wojtyniak and Stone, 1986 | gas phase; switching reaction,Thermochemical ladder((CH3)3Si+)C6H6, Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 146. | J/mol*K | N/A | Wojtyniak and Stone, 1986 | gas phase; switching reaction,Thermochemical ladder((CH3)3Si+)C6H6, Entropy change calculated or estimated; M |
Free energy of reaction
ΔrG° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
43.1 | 468. | PHPMS | Wojtyniak and Stone, 1986 | gas phase; switching reaction,Thermochemical ladder((CH3)3Si+)C6H6, Entropy change calculated or estimated; M |
By formula: Br- + C7H8 = (Br- • C7H8)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 36. ± 7.5 | kJ/mol | IMRE | Paul and Kebarle, 1991 | gas phase; ΔGaff measured at 303 K, corrected to 423 K, ΔSaff taken as that of PhNO2..Br-; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 84. | J/mol*K | N/A | Paul and Kebarle, 1991 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 0.4 ± 4.2 | kJ/mol | IMRE | Paul and Kebarle, 1991 | gas phase; ΔGaff measured at 303 K, corrected to 423 K, ΔSaff taken as that of PhNO2..Br-; B |
Free energy of reaction
ΔrG° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
0.4 | 423. | PHPMS | Paul and Kebarle, 1991 | gas phase; Entropy change calculated or estimated; M |
By formula: C4H9+ + C7H8 = (C4H9+ • C7H8)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 120. | kJ/mol | PHPMS | Stone and Stone, 1991 | gas phase; toluene D8, forms protonated t-butyltoluene; M |
ΔrH° | 122. | kJ/mol | PHPMS | Stone and Stone, 1991 | gas phase; forms protomated t-butyltoluene; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 228. | J/mol*K | PHPMS | Stone and Stone, 1991 | gas phase; toluene D8, forms protonated t-butyltoluene; M |
ΔrS° | 228. | J/mol*K | PHPMS | Stone and Stone, 1991 | gas phase; forms protomated t-butyltoluene; M |
By formula: C7H8+ + C7H8 = (C7H8+ • C7H8)
Bond type: Charge transfer bond (positive ion)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 60.7 | 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° | 66.9 | kJ/mol | PHPMS | Meot-Ner (Mautner), Hamlet, et al., 1978 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 120. | J/mol*K | PHPMS | Meot-Ner (Mautner), Hamlet, et al., 1978 | gas phase; M |
By formula: C6H7N+ + C7H8 = (C6H7N+ • C7H8)
Bond type: Charge transfer bond (positive ion)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 57.3 | kJ/mol | PHPMS | Meot-Ner (Mautner) and El-Shall, 1986 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 109. | J/mol*K | PHPMS | Meot-Ner (Mautner) and El-Shall, 1986 | gas phase; M |
By formula: C9H12+ + C7H8 = (C9H12+ • C7H8)
Bond type: Charge transfer bond (positive ion)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 50.2 | 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- + C7H8 = (NO- • C7H8)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 185. | 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: HBr + C7H7Br = C7H8 + Br2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 33.9 ± 4.2 | kJ/mol | Eqk | Benson and Buss, 1957 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = 33. ± 4. kJ/mol; ALS |
By formula: Cl- + C7H8 = (Cl- • C7H8)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrG° | 16.7 | kJ/mol | TDEq | French, Ikuta, et al., 1982 | gas phase; B |
Free energy of reaction
ΔrG° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
17. | 300. | PHPMS | French, Ikuta, et al., 1982 | gas phase; M |
By formula: HI + C7H7I = C7H8 + I2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -33. ± 4.6 | kJ/mol | Cm | Graham, Nichol, et al., 1955 | liquid phase; solvent: p-Xylene; ALS |
By formula: C7H7Br + 0.5H2 = C7H8 + 0.5Br2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -4. ± 2. | kJ/mol | Chyd | Ashcroft, Carson, et al., 1963 | liquid phase; ALS |
By formula: I- + C7H8 = (I- • C7H8)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 46.0 ± 4.2 | kJ/mol | TDAs | Caldwell, Masucci, et al., 1989 | gas phase; B,M |
By formula: C7H8 = C7H8
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -100. ± 10. | kJ/mol | Cm | Bartmess and Griffith, 1990 | gas phase; Gas phase acidity; ALS |
By formula: C7H7I = C7H8 + 0.5I2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -41. ± 2. | kJ/mol | Chyd | Ashcroft, Carson, et al., 1963 | liquid phase; ALS |
By formula: (Li+ • C7H8) + C7H8 = (Li+ • 2C7H8)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 116. ± 3. | kJ/mol | CIDT | Amunugama and Rodgers, 2002 | RCD |
By formula: (Na+ • C7H8) + C7H8 = (Na+ • 2C7H8)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 87. ± 2. | kJ/mol | CIDT | Amunugama and Rodgers, 2002 | RCD |
By formula: (Cs+ • C7H8) + C7H8 = (Cs+ • 2C7H8)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 61.5 ± 4.2 | kJ/mol | CIDT | Amunugama and Rodgers, 2002 | RCD |
By formula: (Rb+ • C7H8) + C7H8 = (Rb+ • 2C7H8)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 67.8 ± 4.2 | kJ/mol | CIDT | Amunugama and Rodgers, 2002 | RCD |
By formula: (K+ • C7H8) + C7H8 = (K+ • 2C7H8)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 74.9 ± 4.6 | kJ/mol | CIDT | Amunugama and Rodgers, 2002 | RCD |
By formula: (Cr+ • C7H8) + C7H8 = (Cr+ • 2C7H8)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 222. ± 38. | kJ/mol | RAK | Lin and Dunbar, 1997 | RCD |
By formula: C10H14 + C6H6 = C7H8 + C9H12
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 0.0 ± 0.6 | kJ/mol | Eqk | Tsvetkov, Rozhnov, et al., 1985 | liquid phase; ALS |
By formula: Li+ + C7H8 = (Li+ • C7H8)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 183. ± 17. | kJ/mol | CIDT | Amunugama and Rodgers, 2002 | RCD |
By formula: Na+ + C7H8 = (Na+ • C7H8)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 112. ± 3. | kJ/mol | CIDT | Amunugama and Rodgers, 2002 | RCD |
By formula: Cs+ + C7H8 = (Cs+ • C7H8)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 64.0 ± 4.6 | kJ/mol | CIDT | Amunugama and Rodgers, 2002 | RCD |
By formula: Rb+ + C7H8 = (Rb+ • C7H8)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 71.1 ± 4.2 | kJ/mol | CIDT | Amunugama and Rodgers, 2002 | RCD |
By formula: K+ + C7H8 = (K+ • C7H8)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 79.9 ± 5.0 | kJ/mol | CIDT | Amunugama and Rodgers, 2002 | RCD |
By formula: Cr+ + C7H8 = (Cr+ • C7H8)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 176. ± 14. | kJ/mol | RAK | Lin and Dunbar, 1997 | RCD |
References
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Reaction thermochemistry 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]
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]
Schmidlin, 1906
Schmidlin, M.J.,
Recherches chimiques et thermochimiques sur la constitution des rosanilines,
Ann. Chim. Phys., 1906, 1, 195-256. [all data]
Draeger, 1985
Draeger, J.A.,
The methylbenzenes II. Fundamental vibrational shifts, statistical thermodynamic functions, and properties of formation,
J. Chem. Thermodyn., 1985, 17, 263-275. [all data]
Chao J., 1984
Chao J.,
Chemical thermodynamic properties of toluene, o-, m- and p-xylenes,
Thermochim. Acta, 1984, 72, 323-334. [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]
Taylor W.J., 1946
Taylor W.J.,
Heats, equilibrium constants, and free energies of formation of the alkylbenzenes,
J. Res. Nat. Bur. Stand., 1946, 37, 95-122. [all data]
Scott D.W., 1962
Scott D.W.,
Toluene: thermodynamic properties, molecular vibrations, and internal rotation,
J. Phys. Chem., 1962, 66, 911-914. [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]
Scott, Guthrie, et al., 1962
Scott, D.W.; Guthrie, G.B.; Messerly, J.F.; Todd, S.S.; Berg, W.T.; Hossenlopp, I.A.; McCullough, J.P.,
Toluene: thermodynamic properties, molecular vibrations, and internal rotation,
J. Phys. Chem., 1962, 66, 911-914. [all data]
Kelley, 1929
Kelley, K.K.,
The heat capacity of toluene from 14K to 298K. The entropy and the free energy of formation,
J. Am. Chem. Soc., 1929, 51, 2738-2741. [all data]
Grolier, Roux-Desgranges, et al., 1993
Grolier, J.-P.E.; Roux-Desgranges, G.; Berkane, M.; Jimenez, E.; Wilhelm, E.,
Heat capacities and densities of mixtures of very polar substances 2. Mixtures containing N,N-dimethylformamide,
J. Chem. Thermodynam., 1993, 25(1), 41-50. [all data]
Shiohama, Ogawa, et al., 1988
Shiohama, Y.; Ogawa, H.; Murakami, S.; Fujihara, I.,
Excess molar isobaric heat capacities and isentropic compressibilities of (cis- or trans-decalin + benzene or toluene or iso-octane or n-heptane) at 298.15 K,
J. Chem. Thermodynam., 1988, 20, 1183-1189. [all data]
Reddy, 1986
Reddy, K.S.,
Isentropic compressibilities of binary liquid mixtures at 303.15 and 313.15 K,
J. Chem. Eng. Data, 1986, 31, 238-240. [all data]
Roux-Dexgranges, Grolier, et al., 1986
Roux-Dexgranges, G.; Grolier, J.-P.E.; Villamanan, M.A.; Casanova, C.,
Role of alcohol in microemulsions. III. Volumes and heat capacities in the continuious phase water-n-butanol-toluene of reverse micelles,
Fluid Phase Equilibria, 1986, 25, 209-230. [all data]
Tardajos, Aicart, et al., 1986
Tardajos, G.; Aicart, E.; Costas, M.; Patterson, D.,
Liquid structure and second-order mixing functions for benzene, toluene, and p-xylene with n-alkanes, J. Chem. Soc.,
Faraday Trans., 1986, 1 82, 2977-2987. [all data]
Stephens and Olson, 1984
Stephens, M.; Olson, J.D.,
Measurement of excess heat capacities by differential scanning calorimetry,
Thermochim. Acta, 1984, 76, 79-85. [all data]
Grolier, Inglese, et al., 1982
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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 S°liquid Entropy of liquid at standard conditions T Temperature 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 ΔrG° Free energy of reaction at standard conditions ΔrH° Enthalpy of reaction at standard conditions ΔrS° Entropy of reaction at standard conditions - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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