Benzene

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Gas phase thermochemistry data

Go To: Top, Condensed phase thermochemistry data, 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
GT - Glushko Thermocenter, Russian Academy of Sciences, Moscow

Quantity Value Units Method Reference Comment
Δfgas19.8 ± 0.2kcal/molReviewRoux, Temprado, et al., 2008There 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
Δfgas19.8kcal/molN/AGood and Smith, 1969Value 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
Δfgas19.82 ± 0.12kcal/molCcbProsen, Gilmont, et al., 1945Hf by Prosen, Johnson, et al., 1946; ALS
Δfgas19.1kcal/molN/ALandrieu, Baylocq, et al., 1929Value 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
7.95250.Thermodynamics Research Center, 1997GT
8.391100.
10.02150.
12.71200.
17.82273.15
19.70298.15
19.84300.
27.132400.
33.305500.
38.262600.
42.251700.
45.519800.
48.236900.
50.5281000.
52.4761100.
54.1401200.
55.5661300.
56.8001400.
57.8661500.
59.9691750.
61.4872000.
62.6082250.
63.4562500.
64.1092750.
64.6203000.

Constant pressure heat capacity of gas

Cp,gas (cal/mol*K) Temperature (K) Reference Comment
22.30 ± 0.01333.15Todd S.S., 1978Please also see Montgomery J.B., 1942, Pitzer K.S., 1943, Scott D.W., 1947.; GT
22.90341.60
23.42 ± 0.01348.15
24.85 ± 0.01368.15
25.100370.
25.041371.20
26.00 ± 0.30388.
26.501390.
26.40 ± 0.30393.
27.230402.30
27.32 ± 0.02403.15
27.600410.
28.10 ± 0.30417.
28.40 ± 0.30428.
29.491436.15
29.62 ± 0.02438.15
30.30 ± 0.30463.
31.649471.10
31.77 ± 0.02473.15
31.40 ± 0.30481.
33.33 ± 0.02500.15
34.80 ± 0.02527.15

Condensed phase thermochemistry data

Go To: Top, Gas phase thermochemistry data, 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
Δfliquid12. ± 0.2kcal/molReviewRoux, Temprado, et al., 2008There 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
Δfliquid11.70 ± 0.13kcal/molCcbGood and Smith, 1969ALS
Δfliquid11.72 ± 0.12kcal/molCcbProsen, Gilmont, et al., 1945Hf by Prosen, Johnson, et al., 1946; ALS
Δfliquid11.0kcal/molCcbLandrieu, Baylocq, et al., 1929ALS
Quantity Value Units Method Reference Comment
Δcliquid-781. ± 4.kcal/molAVGN/AAverage of 9 values; Individual data points
Quantity Value Units Method Reference Comment
liquid41.410cal/mol*KN/AOliver, Eaton, et al., 1948DH
liquid41.90cal/mol*KN/AHuffman, Parks, et al., 1930Extrapolation below 90 K, 47.49 J/mol*K.; DH
Quantity Value Units Method Reference Comment
solid,1 bar10.89cal/mol*KN/AAhlberg, Blanchard, et al., 1937DH

Constant pressure heat capacity of liquid

Cp,liquid (cal/mol*K) Temperature (K) Reference Comment
32.431298.15Grolier, Roux-Desgranges, et al., 1993DH
32.48298.5Czarnota, 1991p = 0.1 MPa. Cp values given for the pressure range 0.1 to 68.1 MPa.; DH
32.414298.15Lainez, Rodrigo, et al., 1989DH
32.177298.15Shiohama, Ogawa, et al., 1988DH
32.445298.15Grolier, Roux-Desgranges, et al., 1987DH
32.173293.15Kalali, Kohler, et al., 1987T = 293.15, 313.15 K.; DH
32.4348298.15Tanaka, 1987DH
33.44322.05Naziev, Bashirov, et al., 1986T = 322.05, 351.15 K. p = 0.1 MPa. Unsmoothed experimental datum given as 1.7915 kJ/kg*K.; DH
32.84303.15Reddy, 1986T = 303.15, 313.15 K.; DH
32.519298.15Ogawa and Murakami, 1985DH
32.4374298.15Tanaka, 1985DH
32.562298.15Gorbunova, Simonov, et al., 1983T = 283.78 to 348.47 K. Cp = 1.3943 - 5.857x10-4T + 5.89x10-6T2 kJ/kg*K. Cp value calculated from equation.; DH
32.62300.Gorbunova, Grigoriev, et al., 1982T = 280 to 353 K. Data also given by equation.; DH
32.43298.15Grolier, Inglese, et al., 1982T = 298.15 K.; DH
32.443298.15Tanaka, 1982Temperatures 293.15, 298.15, 303.15 K.; DH
32.409298.15Wilhelm, Faradjzadeh, et al., 1982DH
31.93293.15Atalla, El-Sharkawy, et al., 1981DH
32.481298.15Vesely, Zabransky, et al., 1979DH
32.412298.15Grolier, Wilhelm, et al., 1978DH
32.481298.15Vesely, Svoboda, et al., 1977T = 298 to 318 K.; DH
32.409298.15Wilhelm, Grolier, et al., 1977DH
32.447298.15Fortier, Benson, et al., 1976DH
32.4474298.15Fortier and Benson, 1976DH
32.43298.15Rajagopal and Subrahmanyam, 1974T = 298.15 to 323.15 K.; DH
32.10298.Deshpande and Bhatagadde, 1971T = 298 to 318 K.; DH
32.48298.15Hyder Khan and Subrahmanyam, 1971T = 298; 313 K.; DH
32.48298.Subrahmanyam and Khan, 1969DH
32.36298.Recko, 1968T = 24 to 40°C, equation only.; DH
31.1298.Pacor, 1967DH
32.17293.Rastorguev and Ganiev, 1967T = 293 to 353 K.; DH
32.337300.Findenegg, Gruber, et al., 1965DH
32.261298.Rabinovich and Nikolaev, 1962T = 10 to 35°C.; DH
32.29316.Swietoslawski and Zielenkiewicz, 1960Mean value 21 to 66°C.; DH
32.60303.Duff and Everett, 1956T = 303 to 353 K.; DH
32.321298.Staveley, Tupman, et al., 1955T = 288 to 347 K.; DH
7.60293.Sieg, Crtzen, et al., 1951DH
32.519298.15Oliver, Eaton, et al., 1948T = 13 to 337 K.; DH
28.4295.Tschamler, 1948DH
31.91298.Kurbatov, 1947T = 9 to 80°C, mean Cp, five temperatures.; DH
32.50298.1Zhdanov, 1941T = 8 to 46°C.; DH
32.371298.2Burlew, 1940T = 281 to 353 K.; DH
31.41287.8Kolosovskii and Udovenko, 1934DH
31.41287.8de Kolossowsky and Udowenko, 1933DH
31.41298.15Ferguson and Miller, 1933T = 293 to 323 K. Data calculated from equation.; DH
32.29298.1Richards and Wallace, 1932T = 293 to 333 K.; DH
34.314323.15Fiock, Ginnings, et al., 1931T = 50 to 110°C.; DH
32.29300.0Huffman, Parks, et al., 1930T = 93 to 300 K. Value is unsmoothed experimental datum.; DH
31.60298.Andrews, Lynn, et al., 1926T = -18 to 110°C.; DH
31.81293.2Williams and Daniels, 1925T = 20 to 60°C.; DH
32.00303.Willams and Daniels, 1924T = 303 to 333 K. Equation only.; DH
32.79298.Dejardin, 1919T = 24 to 50°C.; DH
31.91298.von Reis, 1881T = 292 to 364 K.; DH

Constant pressure heat capacity of solid

Cp,solid (cal/mol*K) Temperature (K) Reference Comment
11.4490.Ahlberg, Blanchard, et al., 1937T = 4 to 93 K.; DH
23.4223.9Aoyama and Kanda, 1935T = 82 to 224 K. Value is unsmoothed experimental datum.; DH
28.30273.Maass and Walbauer, 1925T = 93 to 273 K.; DH

Phase change 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:
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
Tboil353.3 ± 0.1KAVGN/AAverage of 147 out of 183 values; Individual data points
Quantity Value Units Method Reference Comment
Tfus278.64 ± 0.08KAVGN/AAverage of 57 out of 69 values; Individual data points
Quantity Value Units Method Reference Comment
Ttriple278.5 ± 0.6KAVGN/AAverage of 9 values; Individual data points
Quantity Value Units Method Reference Comment
Tc562.0 ± 0.8KAVGN/AAverage of 36 out of 41 values; Individual data points
Quantity Value Units Method Reference Comment
Pc48.3 ± 0.4atmAVGN/AAverage of 24 out of 26 values; Individual data points
Quantity Value Units Method Reference Comment
Vc0.25 ± 0.03l/molAVGN/AAverage of 6 values; Individual data points
Quantity Value Units Method Reference Comment
ρc3.9 ± 0.2mol/lAVGN/AAverage of 12 values; Individual data points
Quantity Value Units Method Reference Comment
Δvap8.10 ± 0.03kcal/molAVGN/AAverage of 10 out of 11 values; Individual data points
Quantity Value Units Method Reference Comment
Δsub10.6kcal/molTE,MEKruif, 1980Based on data from 183. to 197. K.; AC

Enthalpy of vaporization

ΔvapH (kcal/mol) Temperature (K) Method Reference Comment
7.342353.3N/AMajer and Svoboda, 1985 
7.93320.N/ALubomska, Banas, et al., 2002Based on data from 305. to 345. K.; AC
8.51258. to 313.GCLiu and Dickhut, 1994AC
8.01311.EBAmbrose, Ewing, et al., 1990Based on data from 296. to 377. K.; AC
7.98307.CDong, Lin, et al., 1988AC
7.91314.CDong, Lin, et al., 1988AC
7.74324.CDong, Lin, et al., 1988AC
7.62332.CDong, Lin, et al., 1988AC
7.50344.CDong, Lin, et al., 1988AC
7.31353.CDong, Lin, et al., 1988AC
8.22294.AStephenson and Malanowski, 1987Based on data from 279. to 377. K.; AC
7.53368.AStephenson and Malanowski, 1987Based on data from 353. to 422. K.; AC
7.22435.AStephenson and Malanowski, 1987Based on data from 420. to 502. K.; AC
7.24516.AStephenson and Malanowski, 1987Based on data from 501. to 562. K.; AC
7.36352.N/ANatarajan, 1983AC
7.29361.N/ANatarajan, 1983AC
7.22366.N/ANatarajan, 1983AC
8.44343.N/ATsonopoulos and Wilson, 1983Based on data from 313. to 373. K.; AC
7.4350.N/ARao and Viswanath, 1977AC
7.89 ± 0.02313.CSvoboda, Veselý, et al., 1973AC
7.70 ± 0.02328.CSvoboda, Veselý, et al., 1973AC
7.60 ± 0.02333.CSvoboda, Veselý, et al., 1973AC
7.50 ± 0.02343.CSvoboda, Veselý, et al., 1973AC
7.39 ± 0.02353.CSvoboda, Veselý, et al., 1973AC
7.79 ± 0.1313.DSCMita, Imai, et al., 1971AC
7.8 ± 0.1328.DSCMita, Imai, et al., 1971AC
7.55 ± 0.1345.DSCMita, Imai, et al., 1971AC
8.15299.N/AForziati, Norris, et al., 1949Based on data from 284. to 354. K.; AC
8.15293.N/AYarym-Agaev, Fedos'ev, et al., 1949AC
8.15297.N/AThomson, 1946Based on data from 282. to 354. K.; AC
7.46294.N/AScott and Brickwedde, 1945AC
8.15303.MMWillingham, Taylor, et al., 1945Based on data from 288. to 354. K.; AC
7.98313.EBSmith, 1941Based on data from 298. to 373. K.; AC
8.25288.N/AStuckey and Saylor, 1940Based 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)

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Temperature (K) 293. to 469.
A (kcal/mol) 11.33
α 0.1231
β 0.3602
Tc (K) 562.1
ReferenceMajer and Svoboda, 1985

Antoine Equation Parameters

log10(P) = A − (B / (T + C))
    P = vapor pressure (atm)
    T = temperature (K)

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Temperature (K) A B C Reference Comment
333.4 to 373.54.720121660.652-1.461Eon, Pommier, et al., 1971Coefficents calculated by NIST from author's data.
297.9 to 318.0.1402039.165-261.236Deshpande and Pandya, 1967Coefficents calculated by NIST from author's data.
421.56 to 554.84.597911701.07320.806Kalafati, Rasskazov, et al., 1967Coefficents calculated by NIST from author's data.
287.70 to 354.074.012431203.835-53.226Williamham, Taylor, et al., 1945 

Enthalpy of sublimation

ΔsubH (kcal/mol) Temperature (K) Method Reference Comment
9.97258. to 273.N/ALiu and Dickhut, 1994AC
10.8264.AStephenson and Malanowski, 1987Based on data from 223. to 279. K. See also Ha, Morrison, et al., 1976.; AC
10.8278.N/AHessler, 1984AC
12.9 ± 0.2193.N/ADe Kruif and Van Ginkel, 1977AC
11.8 ± 0.1193.N/ADe Kruif and Van Ginkel, 1977AC
10.9279.MMJackowski, 1974Based on data from 221. to 268. K.; AC
10.5261.N/AJones, 1960AC
10.3229.N/AJones, 1960AC
10.7279.N/AMilazzo, 1956AC
11.1282.AStull, 1947Based on data from 263. to 270. K.; AC
9.2303.VWolf and Weghofer, 1938ALS
10.7273.N/Ade Boer, 1936See also Jackowski, 1974.; AC
10.3226.AMündel, 1913Based on data from 214. to 238. K.; AC

Enthalpy of fusion

ΔfusH (kcal/mol) Temperature (K) Method Reference Comment
2.3581278.69N/AOliver, Eaton, et al., 1948DH
2.370278.65N/AZiegler and Andrews, 1942DH
2.36278.7CDomalski and Hearing, 1996See also Andrews, Lynn, et al., 1926 and Ziegler and Andrews, 1942.; AC
2.223279.1N/ASmith, 1979DH
2.139278.8N/APacor, 1967DH
2.375278.6N/ATschamler, 1948DH
2.343278.6N/AHuffman, Parks, et al., 1930DH
2.360278.55N/AAndrews, Lynn, et al., 1926DH
2.3901278.64N/AMaass and Walbauer, 1925DH

Entropy of fusion

ΔfusS (cal/mol*K) Temperature (K) Reference Comment
8.461278.69Oliver, Eaton, et al., 1948DH
8.506278.65Ziegler and Andrews, 1942DH
7.96279.1Smith, 1979DH
7.67278.8Pacor, 1967DH
8.411278.6Huffman, Parks, et al., 1930DH
8.48278.55Andrews, Lynn, et al., 1926DH
8.58278.64Maass and Walbauer, 1925DH

In addition to the Thermodynamics Research Center (TRC) data available from this site, much more physical and chemical property data is available from the following TRC products:


References

Go To: Top, Gas phase thermochemistry data, 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]

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
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Notes

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