Benzene

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Gas phase thermochemistry data

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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
Δfgas82.9 ± 0.9kJ/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
Δfgas82.8kJ/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
Δfgas82.93 ± 0.50kJ/molCcbProsen, Gilmont, et al., 1945Hf by Prosen, Johnson, et al., 1946; ALS
Δfgas79.9kJ/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 (J/mol*K) Temperature (K) Reference Comment
33.2750.Thermodynamics Research Center, 1997GT
35.11100.
41.94150.
53.17200.
74.55273.15
82.44298.15
83.02300.
113.52400.
139.35500.
160.09600.
176.78700.
190.45800.
201.82900.
211.411000.
219.561100.
226.521200.
232.491300.
237.651400.
242.111500.
250.911750.
257.262000.
261.952250.
265.502500.
268.232750.
270.373000.

Constant pressure heat capacity of gas

Cp,gas (J/mol*K) Temperature (K) Reference Comment
93.32 ± 0.06333.15Todd S.S., 1978Please also see Montgomery J.B., 1942, Pitzer K.S., 1943, Scott D.W., 1947.; GT
95.81341.60
97.99 ± 0.06348.15
103.98 ± 0.06368.15
105.02370.
104.77371.20
108.8 ± 1.3388.
110.88390.
110.5 ± 1.3393.
113.93402.30
114.29 ± 0.07403.15
115.48410.
117.6 ± 1.3417.
118.8 ± 1.3428.
123.39436.15
123.93 ± 0.07438.15
126.8 ± 1.3463.
132.42471.10
132.94 ± 0.08473.15
131.4 ± 1.3481.
139.47 ± 0.08500.15
145.59 ± 0.09527.15

Condensed phase thermochemistry data

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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
Δfliquid49. ± 0.9kJ/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
Δfliquid48.95 ± 0.54kJ/molCcbGood and Smith, 1969ALS
Δfliquid49.04 ± 0.50kJ/molCcbProsen, Gilmont, et al., 1945Hf by Prosen, Johnson, et al., 1946; ALS
Δfliquid46.0kJ/molCcbLandrieu, Baylocq, et al., 1929ALS
Quantity Value Units Method Reference Comment
Δcliquid-3267. ± 20.kJ/molAVGN/AAverage of 9 values; Individual data points
Quantity Value Units Method Reference Comment
liquid173.26J/mol*KN/AOliver, Eaton, et al., 1948DH
liquid175.3J/mol*KN/AHuffman, Parks, et al., 1930Extrapolation below 90 K, 47.49 J/mol*K.; DH
Quantity Value Units Method Reference Comment
solid,1 bar45.56J/mol*KN/AAhlberg, Blanchard, et al., 1937DH

Constant pressure heat capacity of liquid

Cp,liquid (J/mol*K) Temperature (K) Reference Comment
135.69298.15Grolier, Roux-Desgranges, et al., 1993DH
135.9298.5Czarnota, 1991p = 0.1 MPa. Cp values given for the pressure range 0.1 to 68.1 MPa.; DH
135.62298.15Lainez, Rodrigo, et al., 1989DH
134.63298.15Shiohama, Ogawa, et al., 1988DH
135.75298.15Grolier, Roux-Desgranges, et al., 1987DH
134.61293.15Kalali, Kohler, et al., 1987T = 293.15, 313.15 K.; DH
135.707298.15Tanaka, 1987DH
139.9322.05Naziev, Bashirov, et al., 1986T = 322.05, 351.15 K. p = 0.1 MPa. Unsmoothed experimental datum given as 1.7915 kJ/kg*K.; DH
137.4303.15Reddy, 1986T = 303.15, 313.15 K.; DH
136.06298.15Ogawa and Murakami, 1985DH
135.718298.15Tanaka, 1985DH
136.24298.15Gorbunova, 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
136.5300.Gorbunova, Grigoriev, et al., 1982T = 280 to 353 K. Data also given by equation.; DH
135.7298.15Grolier, Inglese, et al., 1982T = 298.15 K.; DH
135.74298.15Tanaka, 1982Temperatures 293.15, 298.15, 303.15 K.; DH
135.60298.15Wilhelm, Faradjzadeh, et al., 1982DH
133.6293.15Atalla, El-Sharkawy, et al., 1981DH
135.90298.15Vesely, Zabransky, et al., 1979DH
135.61298.15Grolier, Wilhelm, et al., 1978DH
135.90298.15Vesely, Svoboda, et al., 1977T = 298 to 318 K.; DH
135.60298.15Wilhelm, Grolier, et al., 1977DH
135.76298.15Fortier, Benson, et al., 1976DH
135.760298.15Fortier and Benson, 1976DH
135.7298.15Rajagopal and Subrahmanyam, 1974T = 298.15 to 323.15 K.; DH
134.3298.Deshpande and Bhatagadde, 1971T = 298 to 318 K.; DH
135.9298.15Hyder Khan and Subrahmanyam, 1971T = 298; 313 K.; DH
135.9298.Subrahmanyam and Khan, 1969DH
135.4298.Recko, 1968T = 24 to 40°C, equation only.; DH
130.298.Pacor, 1967DH
134.6293.Rastorguev and Ganiev, 1967T = 293 to 353 K.; DH
135.30300.Findenegg, Gruber, et al., 1965DH
134.98298.Rabinovich and Nikolaev, 1962T = 10 to 35°C.; DH
135.1316.Swietoslawski and Zielenkiewicz, 1960Mean value 21 to 66°C.; DH
136.4303.Duff and Everett, 1956T = 303 to 353 K.; DH
135.23298.Staveley, Tupman, et al., 1955T = 288 to 347 K.; DH
31.8293.Sieg, Crtzen, et al., 1951DH
136.06298.15Oliver, Eaton, et al., 1948T = 13 to 337 K.; DH
119.295.Tschamler, 1948DH
133.5298.Kurbatov, 1947T = 9 to 80°C, mean Cp, five temperatures.; DH
136.0298.1Zhdanov, 1941T = 8 to 46°C.; DH
135.44298.2Burlew, 1940T = 281 to 353 K.; DH
131.4287.8Kolosovskii and Udovenko, 1934DH
131.4287.8de Kolossowsky and Udowenko, 1933DH
131.4298.15Ferguson and Miller, 1933T = 293 to 323 K. Data calculated from equation.; DH
135.1298.1Richards and Wallace, 1932T = 293 to 333 K.; DH
143.57323.15Fiock, Ginnings, et al., 1931T = 50 to 110°C.; DH
135.1300.0Huffman, Parks, et al., 1930T = 93 to 300 K. Value is unsmoothed experimental datum.; DH
132.2298.Andrews, Lynn, et al., 1926T = -18 to 110°C.; DH
133.1293.2Williams and Daniels, 1925T = 20 to 60°C.; DH
133.9303.Willams and Daniels, 1924T = 303 to 333 K. Equation only.; DH
137.2298.Dejardin, 1919T = 24 to 50°C.; DH
133.5298.von Reis, 1881T = 292 to 364 K.; DH

Constant pressure heat capacity of solid

Cp,solid (J/mol*K) Temperature (K) Reference Comment
47.8690.Ahlberg, Blanchard, et al., 1937T = 4 to 93 K.; DH
97.9223.9Aoyama and Kanda, 1935T = 82 to 224 K. Value is unsmoothed experimental datum.; DH
118.4273.Maass and Walbauer, 1925T = 93 to 273 K.; DH

Phase change data

Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Vibrational and/or electronic energy levels, 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
Pc48.9 ± 0.4barAVGN/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
Δvap33.9 ± 0.1kJ/molAVGN/AAverage of 10 out of 11 values; Individual data points
Quantity Value Units Method Reference Comment
Δsub44.4kJ/molTE,MEKruif, 1980Based on data from 183. to 197. K.; AC

Enthalpy of vaporization

ΔvapH (kJ/mol) Temperature (K) Method Reference Comment
30.72353.3N/AMajer and Svoboda, 1985 
33.2320.N/ALubomska, Banas, et al., 2002Based on data from 305. to 345. K.; AC
35.6258. to 313.GCLiu and Dickhut, 1994AC
33.5311.EBAmbrose, Ewing, et al., 1990Based on data from 296. to 377. K.; AC
33.4307.CDong, Lin, et al., 1988AC
33.1314.CDong, Lin, et al., 1988AC
32.4324.CDong, Lin, et al., 1988AC
31.9332.CDong, Lin, et al., 1988AC
31.4344.CDong, Lin, et al., 1988AC
30.6353.CDong, Lin, et al., 1988AC
34.4294.AStephenson and Malanowski, 1987Based on data from 279. to 377. K.; AC
31.5368.AStephenson and Malanowski, 1987Based on data from 353. to 422. K.; AC
30.2435.AStephenson and Malanowski, 1987Based on data from 420. to 502. K.; AC
30.3516.AStephenson and Malanowski, 1987Based on data from 501. to 562. K.; AC
30.8352.N/ANatarajan, 1983AC
30.5361.N/ANatarajan, 1983AC
30.2366.N/ANatarajan, 1983AC
35.3343.N/ATsonopoulos and Wilson, 1983Based on data from 313. to 373. K.; AC
31.350.N/ARao and Viswanath, 1977AC
33.0 ± 0.1313.CSvoboda, Veselý, et al., 1973AC
32.2 ± 0.1328.CSvoboda, Veselý, et al., 1973AC
31.8 ± 0.1333.CSvoboda, Veselý, et al., 1973AC
31.4 ± 0.1343.CSvoboda, Veselý, et al., 1973AC
30.9 ± 0.1353.CSvoboda, Veselý, et al., 1973AC
32.6 ± 0.4313.DSCMita, Imai, et al., 1971AC
32.5 ± 0.5328.DSCMita, Imai, et al., 1971AC
31.6 ± 0.4345.DSCMita, Imai, et al., 1971AC
34.1299.N/AForziati, Norris, et al., 1949Based on data from 284. to 354. K.; AC
34.1293.N/AYarym-Agaev, Fedos'ev, et al., 1949AC
34.1297.N/AThomson, 1946Based on data from 282. to 354. K.; AC
31.2294.N/AScott and Brickwedde, 1945AC
34.1303.MMWillingham, Taylor, et al., 1945Based on data from 288. to 354. K.; AC
33.4313.EBSmith, 1941Based on data from 298. to 373. K.; AC
34.5288.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) (kJ/mol)
    Tr = reduced temperature (T / Tc)

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Temperature (K) 293. to 469.
A (kJ/mol) 47.41
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 (bar)
    T = temperature (K)

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Temperature (K) A B C Reference Comment
333.4 to 373.54.725831660.652-1.461Eon, Pommier, et al., 1971Coefficents calculated by NIST from author's data.
297.9 to 318.0.1459139.165-261.236Deshpande and Pandya, 1967Coefficents calculated by NIST from author's data.
421.56 to 554.84.603621701.07320.806Kalafati, Rasskazov, et al., 1967Coefficents calculated by NIST from author's data.
287.70 to 354.074.018141203.835-53.226Williamham, Taylor, et al., 1945 

Enthalpy of sublimation

ΔsubH (kJ/mol) Temperature (K) Method Reference Comment
41.7258. to 273.N/ALiu and Dickhut, 1994AC
45.2264.AStephenson and Malanowski, 1987Based on data from 223. to 279. K. See also Ha, Morrison, et al., 1976.; AC
45.1278.N/AHessler, 1984AC
53.9 ± 0.8193.N/ADe Kruif and Van Ginkel, 1977AC
49.4 ± 0.4193.N/ADe Kruif and Van Ginkel, 1977AC
45.6279.MMJackowski, 1974Based on data from 221. to 268. K.; AC
44.1261.N/AJones, 1960AC
43.1229.N/AJones, 1960AC
44.6279.N/AMilazzo, 1956AC
46.6282.AStull, 1947Based on data from 263. to 270. K.; AC
38.303.VWolf and Weghofer, 1938ALS
44.6273.N/Ade Boer, 1936See also Jackowski, 1974.; AC
43.3226.AMündel, 1913Based on data from 214. to 238. K.; AC

Enthalpy of fusion

ΔfusH (kJ/mol) Temperature (K) Method Reference Comment
9.8663278.69N/AOliver, Eaton, et al., 1948DH
9.916278.65N/AZiegler and Andrews, 1942DH
9.87278.7CDomalski and Hearing, 1996See also Andrews, Lynn, et al., 1926 and Ziegler and Andrews, 1942.; AC
9.300279.1N/ASmith, 1979DH
8.950278.8N/APacor, 1967DH
9.937278.6N/ATschamler, 1948DH
9.803278.6N/AHuffman, Parks, et al., 1930DH
9.875278.55N/AAndrews, Lynn, et al., 1926DH
10.000278.64N/AMaass and Walbauer, 1925DH

Entropy of fusion

ΔfusS (J/mol*K) Temperature (K) Reference Comment
35.40278.69Oliver, Eaton, et al., 1948DH
35.59278.65Ziegler and Andrews, 1942DH
33.3279.1Smith, 1979DH
32.1278.8Pacor, 1967DH
35.19278.6Huffman, Parks, et al., 1930DH
35.5278.55Andrews, Lynn, et al., 1926DH
35.9278.64Maass 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:


Vibrational and/or electronic energy levels

Go To: Top, Gas phase thermochemistry data, 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 by: Takehiko Shimanouchi

Symmetry:   D6h     Symmetry Number σ = 12


 Sym.   No   Approximate   Selected Freq.  Infrared   Raman   Comments 
 Species   type of mode   Value   Rating   Value  Phase  Value  Phase

a1g 1 CH str 3062  C  ia 3061.9 VS p liq.
a1g 2 Ring str 992  C  ia 991.6 VS p liq.
a2g 3 CH bend 1326  E  ia 1326 VW liq.
a2u 4 CH bend 673  B 673 S gas  ia
b1u 5 CH str 3068  C 3067.57 VW sln.  ia
b1u 6 Ring deform 1010  C 1010 W sln.  ia
b2g 7 CH bend 995  E  ia  ia OC197207)
b2g 8 Ring deform 703  E  ia  ia OC198, ν208)
b2u 9 Ring str 1310  C 1310 W liq.  ia
b2u 10 CH bend 1150  C 1150 W liq.  ia
e1g 11 CH bend 849  C  ia 848.9 M dp liq.
e1u 12 CH str 3063  E 3080 S liq.  ia FR1316)
e1u 12 CH str 3063  E 3030 S liq.  ia FR1316)
e1u 13 Ring str + deform 1486  B 1486 S gas  ia
e1u 14 CH bend 1038  B 1038 S gas  ia
e2g 15 CH str 3047  C  ia 3046.8 S dp liq.
e2g 16 Ring str 1596  E  ia 1606.4 S dp liq. FR218)
e2g 16 Ring str 1596  E  ia 1584.6 S dp liq. FR218)
e2g 17 CH bend 1178  C  ia 1178.0 S dp liq.
e2g 18 Ring deform 606  C  ia 605.6 S dp liq.
e2u 19 CH bend 975  C 975 W liq.  ia
e2u 20 Ring deform 410  C 417.7 S sln.  ia
e2u 20 Ring deform 410  C 403.0 S sln.  ia

Source: Shimanouchi, 1972

Notes

VSVery strong
SStrong
MMedium
WWeak
VWVery weak
iaInactive
pPolarized
dpDepolarized
FRFermi resonance with an overtone or a combination tone indicated in the parentheses.
OCFrequency estimated from an overtone or a combination tone indicated in the parentheses.
B1~3 cm-1 uncertainty
C3~6 cm-1 uncertainty
E15~30 cm-1 uncertainty

References

Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Vibrational and/or electronic energy levels, 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
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Notes

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