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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- Information on this page:
- Other data available:
- Gas phase thermochemistry data
- Reaction thermochemistry data: reactions 1 to 50, reactions 51 to 99
- Henry's Law data
- Gas phase ion energetics data
- Ion clustering data
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- Vibrational and/or electronic energy levels
- Gas Chromatography
- Fluid Properties
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Condensed phase thermochemistry data
Go To: Top, Phase change data, References, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data compiled as indicated in comments:
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 |
Phase change data
Go To: Top, Condensed phase thermochemistry data, References, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data compiled as indicated in comments:
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, Chris Muzny director
BS - Robert L. Brown and Stephen E. Stein
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)
View plot Requires a JavaScript / HTML 5 canvas capable browser.
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)
View plot Requires a JavaScript / HTML 5 canvas capable browser.
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 |
References
Go To: Top, Condensed phase thermochemistry data, Phase change data, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
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]
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]
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Notes
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- Symbols used in this document:
Cp,liquid Constant pressure heat capacity of liquid Cp,solid Constant pressure heat capacity of solid Pc Critical pressure S°liquid Entropy of liquid at standard conditions S°solid,1 bar Entropy of solid at standard conditions (1 bar) Tboil Boiling point Tc Critical temperature Tfus Fusion (melting) point Ttriple Triple point temperature Vc Critical volume ΔcH°liquid Enthalpy of combustion of liquid at standard conditions ΔfH°liquid Enthalpy of formation of liquid at standard conditions ΔfusH Enthalpy of fusion ΔfusS Entropy of fusion 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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