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
View 3d structure (requires JavaScript / HTML 5) - 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, Condensed phase thermochemistry 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 | 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 |
Condensed phase thermochemistry data
Go To: Top, Gas phase thermochemistry 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
DH - Eugene S. Domalski and Elizabeth D. Hearing
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°liquid | 49. ± 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°liquid | 48.95 ± 0.54 | kJ/mol | Ccb | Good and Smith, 1969 | ALS |
ΔfH°liquid | 49.04 ± 0.50 | kJ/mol | Ccb | Prosen, Gilmont, et al., 1945 | Hf by Prosen, Johnson, et al., 1946; ALS |
ΔfH°liquid | 46.0 | kJ/mol | Ccb | Landrieu, Baylocq, et al., 1929 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -3267. ± 20. | kJ/mol | AVG | N/A | Average of 9 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
S°liquid | 173.26 | J/mol*K | N/A | Oliver, Eaton, et al., 1948 | DH |
S°liquid | 175.3 | J/mol*K | N/A | Huffman, Parks, et al., 1930 | Extrapolation below 90 K, 47.49 J/mol*K.; DH |
Quantity | Value | Units | Method | Reference | Comment |
S°solid,1 bar | 45.56 | J/mol*K | N/A | Ahlberg, Blanchard, et al., 1937 | DH |
Constant pressure heat capacity of liquid
Cp,liquid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
135.69 | 298.15 | Grolier, Roux-Desgranges, et al., 1993 | DH |
135.9 | 298.5 | Czarnota, 1991 | p = 0.1 MPa. Cp values given for the pressure range 0.1 to 68.1 MPa.; DH |
135.62 | 298.15 | Lainez, Rodrigo, et al., 1989 | DH |
134.63 | 298.15 | Shiohama, Ogawa, et al., 1988 | DH |
135.75 | 298.15 | Grolier, Roux-Desgranges, et al., 1987 | DH |
134.61 | 293.15 | Kalali, Kohler, et al., 1987 | T = 293.15, 313.15 K.; DH |
135.707 | 298.15 | Tanaka, 1987 | DH |
139.9 | 322.05 | Naziev, Bashirov, et al., 1986 | T = 322.05, 351.15 K. p = 0.1 MPa. Unsmoothed experimental datum given as 1.7915 kJ/kg*K.; DH |
137.4 | 303.15 | Reddy, 1986 | T = 303.15, 313.15 K.; DH |
136.06 | 298.15 | Ogawa and Murakami, 1985 | DH |
135.718 | 298.15 | Tanaka, 1985 | DH |
136.24 | 298.15 | Gorbunova, Simonov, et al., 1983 | T = 283.78 to 348.47 K. Cp = 1.3943 - 5.857x10-4T + 5.89x10-6T2 kJ/kg*K. Cp value calculated from equation.; DH |
136.5 | 300. | Gorbunova, Grigoriev, et al., 1982 | T = 280 to 353 K. Data also given by equation.; DH |
135.7 | 298.15 | Grolier, Inglese, et al., 1982 | T = 298.15 K.; DH |
135.74 | 298.15 | Tanaka, 1982 | Temperatures 293.15, 298.15, 303.15 K.; DH |
135.60 | 298.15 | Wilhelm, Faradjzadeh, et al., 1982 | DH |
133.6 | 293.15 | Atalla, El-Sharkawy, et al., 1981 | DH |
135.90 | 298.15 | Vesely, Zabransky, et al., 1979 | DH |
135.61 | 298.15 | Grolier, Wilhelm, et al., 1978 | DH |
135.90 | 298.15 | Vesely, Svoboda, et al., 1977 | T = 298 to 318 K.; DH |
135.60 | 298.15 | Wilhelm, Grolier, et al., 1977 | DH |
135.76 | 298.15 | Fortier, Benson, et al., 1976 | DH |
135.760 | 298.15 | Fortier and Benson, 1976 | DH |
135.7 | 298.15 | Rajagopal and Subrahmanyam, 1974 | T = 298.15 to 323.15 K.; DH |
134.3 | 298. | Deshpande and Bhatagadde, 1971 | T = 298 to 318 K.; DH |
135.9 | 298.15 | Hyder Khan and Subrahmanyam, 1971 | T = 298; 313 K.; DH |
135.9 | 298. | Subrahmanyam and Khan, 1969 | DH |
135.4 | 298. | Recko, 1968 | T = 24 to 40°C, equation only.; DH |
130. | 298. | Pacor, 1967 | DH |
134.6 | 293. | Rastorguev and Ganiev, 1967 | T = 293 to 353 K.; DH |
135.30 | 300. | Findenegg, Gruber, et al., 1965 | DH |
134.98 | 298. | Rabinovich and Nikolaev, 1962 | T = 10 to 35°C.; DH |
135.1 | 316. | Swietoslawski and Zielenkiewicz, 1960 | Mean value 21 to 66°C.; DH |
136.4 | 303. | Duff and Everett, 1956 | T = 303 to 353 K.; DH |
135.23 | 298. | Staveley, Tupman, et al., 1955 | T = 288 to 347 K.; DH |
31.8 | 293. | Sieg, Crtzen, et al., 1951 | DH |
136.06 | 298.15 | Oliver, Eaton, et al., 1948 | T = 13 to 337 K.; DH |
119. | 295. | Tschamler, 1948 | DH |
133.5 | 298. | Kurbatov, 1947 | T = 9 to 80°C, mean Cp, five temperatures.; DH |
136.0 | 298.1 | Zhdanov, 1941 | T = 8 to 46°C.; DH |
135.44 | 298.2 | Burlew, 1940 | T = 281 to 353 K.; DH |
131.4 | 287.8 | Kolosovskii and Udovenko, 1934 | DH |
131.4 | 287.8 | de Kolossowsky and Udowenko, 1933 | DH |
131.4 | 298.15 | Ferguson and Miller, 1933 | T = 293 to 323 K. Data calculated from equation.; DH |
135.1 | 298.1 | Richards and Wallace, 1932 | T = 293 to 333 K.; DH |
143.57 | 323.15 | Fiock, Ginnings, et al., 1931 | T = 50 to 110°C.; DH |
135.1 | 300.0 | Huffman, Parks, et al., 1930 | T = 93 to 300 K. Value is unsmoothed experimental datum.; DH |
132.2 | 298. | Andrews, Lynn, et al., 1926 | T = -18 to 110°C.; DH |
133.1 | 293.2 | Williams and Daniels, 1925 | T = 20 to 60°C.; DH |
133.9 | 303. | Willams and Daniels, 1924 | T = 303 to 333 K. Equation only.; DH |
137.2 | 298. | Dejardin, 1919 | T = 24 to 50°C.; DH |
133.5 | 298. | von Reis, 1881 | T = 292 to 364 K.; DH |
Constant pressure heat capacity of solid
Cp,solid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
47.86 | 90. | Ahlberg, Blanchard, et al., 1937 | T = 4 to 93 K.; DH |
97.9 | 223.9 | Aoyama and Kanda, 1935 | T = 82 to 224 K. Value is unsmoothed experimental datum.; DH |
118.4 | 273. | Maass and Walbauer, 1925 | T = 93 to 273 K.; DH |
Gas phase ion energetics 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 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) | 750.4 | kJ/mol | N/A | Hunter and Lias, 1998 | HL |
Quantity | Value | Units | Method | Reference | Comment |
Gas basicity | 725.4 | kJ/mol | N/A | Hunter and Lias, 1998 | HL |
Proton affinity at 298K
Proton affinity (kJ/mol) | Reference | Comment |
---|---|---|
746.4 | 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) (kJ/mol) | Reference | Comment |
---|---|---|
721.7 | 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° | 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 |
References
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry 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]
Oliver, Eaton, et al., 1948
Oliver, G.D.; Eaton, M.; Huffman, H.M.,
The heat capacity, heat of fusion and entropy of benzene,
J. Am. Chem. Soc., 1948, 70, 1502-1505. [all data]
Huffman, Parks, et al., 1930
Huffman, H.M.; Parks, G.S.; Daniels, A.C.,
Thermal data on organic compounds. VII. The heat capacities, entropies and free energies of twelve aromatic hydrocarbons,
J. Am. Chem. Soc., 1930, 52, 1547-1558. [all data]
Ahlberg, Blanchard, et al., 1937
Ahlberg, J.E.; Blanchard, E.R.; Lundberg, W.O.,
The heat capacities of benzene, methyl alcohol and glycerol at very low temperatures,
J. Chem. Phys., 1937, 5, 537-551. [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]
Czarnota, 1991
Czarnota, I.,
Heat capacity of benzene at high pressures,
J. Chem. Thermodynam., 1991, 23, 25-30. [all data]
Lainez, Rodrigo, et al., 1989
Lainez, A.; Rodrigo, M.M.; Wilhelm, E.; Grolier, J.-P.E.,
Excess volumes and excess heaat capacitiies of some mixtures with trans,trans,cis-1,5,9-cyclododecatriene at 298.15K,
J. Chem. Eng. Data, 1989, 34, 332-335. [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]
Grolier, Roux-Desgranges, et al., 1987
Grolier, J.-P.E.; Roux-Desgranges, G.; Kooner, Z.S.; Smith, J.F.; Hepler, L.G.,
Thermal and volumetric properties of chloroform + benzene mixtures and the ideal associated solution model of complex formation,
J. Solution Chem., 1987, 16, 745-752. [all data]
Kalali, Kohler, et al., 1987
Kalali, H.; Kohler, F.; Svejda, P.,
Excess properties of the mixture bis(2-dichlorethyl)ether (chlorex) + 2,2,4-trimethylpentane (isooctane),
Monatsh. Chem., 1987, 118, 1-18. [all data]
Tanaka, 1987
Tanaka, R.,
Excess heat capacities for mixture of benzene with n-heptane at 293.15, 298.15 and 303.15 K,
J. Chem. Eng. Data, 1987, 32, 176-177. [all data]
Naziev, Bashirov, et al., 1986
Naziev, Ya.M.; Bashirov, M.M.; Badalov, Yu.A.,
Experimental device for measurement of isobaric specific heat of electrolytes at elevated pressures,
Inzh-Fiz. Zhur., 1986, 51(5), 789-795. [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]
Ogawa and Murakami, 1985
Ogawa, H.; Murakami, S.,
Flow microcalorimeter for heat capacities of solutions,
Thermochim. Acta, 1985, 88, 255-260. [all data]
Tanaka, 1985
Tanaka, R.,
Excess heat capacities for mixtures of benzene with cyclopentane, methylcyclohexane, and cyclooctane at 298.15 K,
J. Chem. Eng. Data, 1985, 30, 267-269. [all data]
Gorbunova, Simonov, et al., 1983
Gorbunova, N.I.; Simonov, V.M.; Shipova, V.A.,
Thermodynamic properties of benzene,
Teplofiz. Vys. Temp., 1983, 21(2), 270-275. [all data]
Gorbunova, Grigoriev, et al., 1982
Gorbunova, N.I.; Grigoriev, V.A.; Simonov, V.M.; Shipova, V.A.,
Heat capacity of liquid benzene and hexafluorobenzene at atmospheric pressure,
Int. J. Thermophysics, 1982, 3, 1-15. [all data]
Grolier, Inglese, et al., 1982
Grolier, J.-P.E.; Inglese, A.; Wilhelm, E.,
Excess volumes and excess heat capacities of tetrachloroethene + cyclohexane, + methylcyclohexane, + benzene, and + toluene at 298.15 K,
J. Chem. Thermodynam., 1982, 14, 523-529. [all data]
Tanaka, 1982
Tanaka, R.,
Determination of excess heat capacities of (benzene + tetrachloromethane and + cyclohexane) between 293.15 and 303.15 K by use of a Picker flow calorimeter,
J. Chem. Thermodynam., 1982, 14, 259-268. [all data]
Wilhelm, Faradjzadeh, et al., 1982
Wilhelm, E.; Faradjzadeh, A.; Grolier, J.-P.E.,
Excess volumes and excess heat capacities of 2,3-dimethylbutane + butane and + toluene,
J. Chem. Thermodynam., 1982, 14, 1199-1200. [all data]
Atalla, El-Sharkawy, et al., 1981
Atalla, S.R.; El-Sharkawy, A.A.; Gasser, F.A.,
Measurement of thermal properties of liquids with an AC heated-wire technique,
Inter. J. Thermophys., 1981, 2(2), 155-162. [all data]
Vesely, Zabransky, et al., 1979
Vesely, F.; Zabransky, M.; Svoboda, V.; Pick, J.,
The use of mixing calorimeter for measuring heat capacities of liquids,
Coll. Czech. Chem. Commun., 1979, 44, 3529-3532. [all data]
Grolier, Wilhelm, et al., 1978
Grolier, J.-P.E.; Wilhelm, E.; Hamedi, M.H.,
Molar heat capacities and isothermal compressibility of binary liquid mixtures: carbon tetrachloride + benzene, carbon tetrachloride + cyclohexane and benzene + cyclohexane,
Ber. Bunsenges. Phys. Chem., 1978, 82, 1282-1290. [all data]
Vesely, Svoboda, et al., 1977
Vesely, F.; Svoboda, V.; Pick, J.,
Heat capacities of some organic liquids determined with the mixing calorimeter,
1st Czech. Conf. Calorimetry (Lect. Short Commun.), 1977, C9-1-C9-4. [all data]
Wilhelm, Grolier, et al., 1977
Wilhelm, E.; Grolier, J.-P.E.; Karbalai Ghassemi, M.H.,
Molar heat capacities of binary liquid mixtures: 1,2-dichloroethane + benzene, + toluene, and + p-xylene,
Ber. Bunsenges. Phys. Chem., 1977, 81, 925-930. [all data]
Fortier, Benson, et al., 1976
Fortier, J.-L.; Benson, G.C.; Picker, P.,
Heat capacities of some organic liquids determined with the Picker flow calorimeter,
J. Chem. Thermodynam., 1976, 8, 289-299. [all data]
Fortier and Benson, 1976
Fortier, J.-L.; Benson, G.C.,
Excess heat capacities of binary liquid mixtures determined with a Picker flow calorimeter,
J. Chem. Thermodynam., 1976, 8, 411-423. [all data]
Rajagopal and Subrahmanyam, 1974
Rajagopal, E.; Subrahmanyam, S.V.,
Excess function of VE,(dVE/dp)T, and CpE of isooctane + benzene and + toluene,
J. Chem. Thermodynam., 1974, 6, 873-876. [all data]
Deshpande and Bhatagadde, 1971
Deshpande, D.D.; Bhatagadde, L.G.,
Heat capacities at constant volume, free volumes, and rotational freedom in some liquids,
Aust. J. Chem., 1971, 24, 1817-1822. [all data]
Hyder Khan and Subrahmanyam, 1971
Hyder Khan, V.; Subrahmanyam, S.V.,
Excess thermodynamic functions of the systems: benzene + p-xylene and benzene + p-dioxan,
Trans. Faraday Soc., 1971, 67, 2282-2291. [all data]
Subrahmanyam and Khan, 1969
Subrahmanyam, S.V.; Khan, V.H.,
Thermodynamics of the system benzene - p-dioxane,
Curr. Sci., 1969, 38, 510-511. [all data]
Recko, 1968
Recko, W.M.,
Excess heat capacity of the binary systems formed by n-propyl alcohol with benzene, mesitylene and cyclohexane,
Bull. Acad. Pol. Sci. Ser. Sci. Chim., 1968, 16, 549-552. [all data]
Pacor, 1967
Pacor, P.,
Applicability of the DuPont 900 DTA apparatus in quantitative differential thermal analysis,
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Rastorguev and Ganiev, 1967
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Notes
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- Symbols used in this document:
AE Appearance energy Cp,gas Constant pressure heat capacity of gas Cp,liquid Constant pressure heat capacity of liquid Cp,solid Constant pressure heat capacity of solid IE (evaluated) Recommended ionization energy S°liquid Entropy of liquid at standard conditions S°solid,1 bar Entropy of solid at standard conditions (1 bar) 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 - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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