Cyclohexane

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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:
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
Δfliquid-157.7 ± 1.8kJ/molCcbSpitzer and Huffman, 1947ALS
Δfliquid-156.2 ± 0.79kJ/molCcbProsen, Johnson, et al., 1946ALS
Δfliquid-156.4 ± 1.3kJ/molCcbMoore, Renquist, et al., 1940Reanalyzed by Cox and Pilcher, 1970, Original value = -157.7 kJ/mol; ALS
Quantity Value Units Method Reference Comment
Δcliquid-3930. ± 20.kJ/molAVGN/AAverage of 7 values; Individual data points
Quantity Value Units Method Reference Comment
liquid203.89J/mol*KN/AAston, Szasa, et al., 1943DH
liquid204.35J/mol*KN/ARuehrwein and Huffman, 1943DH
liquid205.9J/mol*KN/AParks, Huffman, et al., 1930Extrapolation below 90 K, 50.54 J/mol*K.; DH

Constant pressure heat capacity of liquid

Cp,liquid (J/mol*K) Temperature (K) Reference Comment
156.00298.15Trejo, Costas, et al., 1991DH
156.90298.15Lainez, Rodrigo, et al., 1989DH
143.9326.5Voss and Sloan, 1989T = 326.5 to 450.0 K. Unsmoothed experimental datum.; DH
155.96298.15Saito and Tanaka, 1988DH
154.32298.15Shiohama, Ogawa, et al., 1988DH
155.13293.15Kalali, Kohler, et al., 1987T = 293.15, 313.15 K.; DH
157.06298.15Jimenez, Romani, et al., 1986DH
155.85298.15Ortega, 1986DH
156.5298.15Nkinamubanzi, Charlet, et al., 1985DH
155.96298.15Tanaka, Nakamichi, et al., 1985DH
154.81293.15Siddiqi, Svejda, et al., 1983DH
156.4298.15Grolier, Inglese, et al., 1982DH
156.0298.15Tanaka, 1982T = 293.15, 298.15, 303.15 K. Data at three temperatures.; DH
156.149298.15Fortier, D'Arcy, et al., 1979DH
156.12298.15Vesely, Zabransky, et al., 1979DH
156.4298.15Wilhelm, Grolier, et al., 1979DH
156.35298.15Grolier, Wilhelm, et al., 1978DH
156.7298.Safir, 1978T = 298 to 313 K. Data calculated from equation Cp = 1.7493 + 0.00452 T kJ/kg*K.; DH
156.12298.15Vesely, Svoboda, et al., 1977T = 298 to 318 K.; DH
156.07298.15Fortier, Benson, et al., 1976DH
156.070298.15Fortier and Benson, 1976DH
156.20298.15Jolicoeur, Boileau, et al., 1975DH
154.80293.15Wilhelm, Zettler, et al., 1974T = 273 to 323 K.; DH
159.6298.15Subrahmanyam and Rajagopal, 1973T = 298 to 323 K.; DH
155.2298.15Wilhelm, Schano, et al., 1969Temperature 20, 30, and 40°C.; DH
155.5298.Recko, 1968T = 24 to 40°C, equation only.; DH
152.93298.Nikolaev, Rabinovich, et al., 1966T = 10 to 50°C.; DH
155.31298.00Moelwyn-Hughes and Thorpe, 1964T = 297 to 327 K.; DH
155.2311.Swietoslawski and Zielenkiewicz, 1960Mean value 20 to 56°C.; DH
154.2300.Auerbach, Sage, et al., 1950T = 300 to 366 K. Cp given as 0.4378 Btu/lb*R at 80°F.; DH
155.85295.Aston, Szasa, et al., 1943T = 12 to 293 K.; DH
156.31298.15Ruehrwein and Huffman, 1943T = 13 to 302 K.; DH
100.4304.2Phillip, 1939DH
143.9298.9Parks, Huffman, et al., 1930T = 92 to 299 K. Value is unsmoothed experimental datum.; DH
176.1298.Dejardin, 1919T = 22 to 50°C.; 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
AC - William E. Acree, Jr., James S. Chickos
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
DRB - Donald R. Burgess, Jr.
DH - Eugene S. Domalski and Elizabeth D. Hearing
CAL - James S. Chickos, William E. Acree, Jr., Joel F. Liebman, Students of Chem 202 (Introduction to the Literature of Chemistry), University of Missouri -- St. Louis

Quantity Value Units Method Reference Comment
Tboil353.9 ± 0.2KAVGN/AAverage of 93 out of 116 values; Individual data points
Quantity Value Units Method Reference Comment
Tfus279.6 ± 0.3KAVGN/AAverage of 38 out of 47 values; Individual data points
Quantity Value Units Method Reference Comment
Ttriple279.7 ± 0.4KAVGN/AAverage of 8 values; Individual data points
Quantity Value Units Method Reference Comment
Tc554. ± 1.KAVGN/AAverage of 18 values; Individual data points
Quantity Value Units Method Reference Comment
Pc40.7 ± 0.5barAVGN/AAverage of 8 values; Individual data points
Quantity Value Units Method Reference Comment
Vc0.308l/molN/ADaubert, 1996 
Vc0.309l/molN/AYoung, 1972Uncertainty assigned by TRC = 0.003 l/mol; TRC
Quantity Value Units Method Reference Comment
ρc3.24 ± 0.03mol/lN/ADaubert, 1996 
ρc3.26mol/lN/ATeja and Anselme, 1990Uncertainty assigned by TRC = 0.07 mol/l; TRC
ρc3.230mol/lN/ASimon, 1957Uncertainty assigned by TRC = 0.04 mol/l; TRC
ρc3.250mol/lN/AYoung, 1910Uncertainty assigned by TRC = 0.02 mol/l; TRC
ρc3.247mol/lN/AYoung and Fortey, 1899Uncertainty assigned by TRC = 0.06 mol/l; TRC
Quantity Value Units Method Reference Comment
Δvap33.1 ± 0.4kJ/molAVGN/AAverage of 19 out of 21 values; Individual data points

Enthalpy of vaporization

ΔvapH (kJ/mol) Temperature (K) Method Reference Comment
29.97353.9N/AMajer and Svoboda, 1985 
33.334298.15N/AAston, Szasa, et al., 1943P = 13.18 kPa; DH
33.1315.EBGierycz, Kosowski, et al., 2009Based on data from 296. to 353. K.; AC
32.7315.N/ALubomska, Banas, et al., 2002Based on data from 300. to 345. K.; AC
31.9324.EBDiogo, Santos, et al., 1995Based on data from 313. to 336. K.; AC
32.2375.N/ALee and Holder, 1993Based on data from 360. to 470. K.; AC
32.3314.CDong, Lin, et al., 1988AC
31.1332.CDong, Lin, et al., 1988AC
30.3345.CDong, Lin, et al., 1988AC
30.0355.CDong, Lin, et al., 1988AC
30.9368.AStephenson and Malanowski, 1987Based on data from 353. to 414. K.; AC
29.6427.AStephenson and Malanowski, 1987Based on data from 412. to 491. K.; AC
29.6504.AStephenson and Malanowski, 1987Based on data from 489. to 553. K.; AC
32.9308.A,MMStephenson and Malanowski, 1987Based on data from 293. to 355. K. See also Willingham, Taylor, et al., 1945.; AC
32.3 ± 0.1313.CMajer, Svoboda, et al., 1979AC
31.2 ± 0.1333.CMajer, Svoboda, et al., 1979AC
31.0 ± 0.1338.CMajer, Svoboda, et al., 1979AC
30.4 ± 0.1348.CMajer, Svoboda, et al., 1979AC
30.1 ± 0.1353.CMajer, Svoboda, et al., 1979AC
32.2 ± 0.1313.CSvoboda, Veselý, et al., 1973AC
31.9 ± 0.1323.CSvoboda, Veselý, et al., 1973AC
31.1 ± 0.1333.CSvoboda, Veselý, et al., 1973AC
30.6 ± 0.1343.CSvoboda, Veselý, et al., 1973AC
30.1 ± 0.1354.CSvoboda, Veselý, et al., 1973AC
32.5318.N/AGaw and Swinton, 1968Based on data from 303. to 343. K.; AC
32.9313.N/ACruickshank and Cutler, 1967Based on data from 298. to 348. K.; AC
32.8331.N/AMarinichev and Susarev, 1965Based on data from 316. to 354. K.; AC
31.4 ± 0.1324.CMcCullough, Person, et al., 1951AC
30.4 ± 0.1346.CMcCullough, Person, et al., 1951AC
30.1354.N/ASpitzer and Pitzer, 1946AC

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) 292. to 422.
A (kJ/mol) 43.32
α -0.1437
β 0.4512
Tc (K) 553.4
ReferenceMajer and Svoboda, 1985

Entropy of vaporization

ΔvapS (J/mol*K) Temperature (K) Reference Comment
111.80298.15Aston, Szasa, et al., 1943P; DH

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
323. to 523.4.139831316.554-35.581Kerns, Anthony, et al., 1974Coefficents calculated by NIST from author's data.
303. to 343.3.99201216.93-48.621Gaw and Swinton, 1968, 2Coefficents calculated by NIST from author's data.
315.70 to 353.903.17125780.637-107.29Marinichev and Susarev, 1965, 2Coefficents calculated by NIST from author's data.
293.06 to 354.733.969881203.526-50.287Williamham, Taylor, et al., 1945 

Enthalpy of sublimation

ΔsubH (kJ/mol) Temperature (K) Method Reference Comment
27.6265.AStephenson and Malanowski, 1987Based on data from 223. to 280. K.; AC
46.6186.BBondi, 1963AC
37.2273.N/AJones, 1960Based on data from 268. to 278. K.; AC
37.7248.AStull, 1947Based on data from 228. to 268. K.; AC
36.5274.ARotinjanz and Nagornow, 1934Based on data from 269. to 279. K.; AC

Enthalpy of fusion

ΔfusH (kJ/mol) Temperature (K) Reference Comment
2.68279.8Domalski and Hearing, 1996AC

Entropy of fusion

ΔfusS (J/mol*K) Temperature (K) Reference Comment
36.2186.1Domalski and Hearing, 1996CAL
9.57279.8

Enthalpy of phase transition

ΔHtrs (kJ/mol) Temperature (K) Initial Phase Final Phase Reference Comment
6.686186.09crystaline, IIcrystaline, IAston, Szasa, et al., 1943DH
2.628279.84crystaline, IliquidAston, Szasa, et al., 1943DH
6.7396186.1crystaline, IIcrystaline, IRuehrwein and Huffman, 1943DH
2.6769279.82crystaline, IliquidRuehrwein and Huffman, 1943DH
6.820186.4crystaline, IIcrystaline, IZiegler and Andrews, 1942DH
2.728279.4crystaline, IliquidZiegler and Andrews, 1942DH
6.234185.9crystaline, IIcrystaline, IParks, Huffman, et al., 1930DH
2.423279.3crystaline, IliquidParks, Huffman, et al., 1930DH

Entropy of phase transition

ΔStrs (J/mol*K) Temperature (K) Initial Phase Final Phase Reference Comment
35.93186.09crystaline, IIcrystaline, IAston, Szasa, et al., 1943DH
9.39279.84crystaline, IliquidAston, Szasa, et al., 1943DH
36.21186.1crystaline, IIcrystaline, IRuehrwein and Huffman, 1943DH
9.57279.82crystaline, IliquidRuehrwein and Huffman, 1943DH
36.59186.4crystaline, IIcrystaline, IZiegler and Andrews, 1942DH
9.76279.4crystaline, IliquidZiegler and Andrews, 1942DH
33.53185.9crystaline, IIcrystaline, IParks, Huffman, et al., 1930DH
8.68279.3crystaline, IliquidParks, Huffman, et al., 1930DH

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, 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.

Spitzer and Huffman, 1947
Spitzer, R.; Huffman, H.M., The heats of combustion of cyclopentane, cyclohexane, cycloheptane and cyclooctane, J. Am. Chem. Soc., 1947, 69, 211-213. [all data]

Prosen, Johnson, et al., 1946
Prosen, E.J.; Johnson, W.H.; Rossini, F.D., Heats of formation and combustion of the normal alkylcyclopentanes and cyclohexanes and the increment per CH2 group for several homologous series of hydrocarbons, J. Res. NBS, 1946, 37, 51-56. [all data]

Moore, Renquist, et al., 1940
Moore, G.E.; Renquist, M.L.; Parks, G.S., Thermal data on organic compounds. XX. Modern combustion data for two methylnonanes, methyl ethyl ketone, thiophene and six cycloparaffins, J. Am. Chem. Soc., 1940, 62, 1505-1507. [all data]

Cox and Pilcher, 1970
Cox, J.D.; Pilcher, G., Thermochemistry of Organic and Organometallic Compounds, Academic Press, New York, 1970, 1-636. [all data]

Aston, Szasa, et al., 1943
Aston, J.G.; Szasa, G.J.; Fink, H.L., The heat capacity and entropy, heats of transition, fusion and vaporization and the vapor pressures of cyclohexane. The vibrational frequencies of alicyclic ring systems, J. Am. Chem. Soc., 1943, 65, 1135-1139. [all data]

Ruehrwein and Huffman, 1943
Ruehrwein, R.A.; Huffman, H.M., Thermal data. XVII. The heat capacity, entropy and free energy of formation of cyclohexane. A new method of heat transfer in low temperature calorimetry, J. Am. Chem. Soc., 1943, 65, 1620-1625. [all data]

Parks, Huffman, et al., 1930
Parks, G.S.; Huffman, H.M.; Thomas, S.B., Thermal data on organic compounds. VI. The heat capacities, entropies and free energies of some saturated, non-benzenoid hydrocarbons, J. Am. Chem. Soc., 1930, 52, 1032-1041. [all data]

Trejo, Costas, et al., 1991
Trejo, L.M.; Costas, M.; Patterson, D., Excess heat capacity of organic mixtures, Internat. DATA Series, Selected Data Mixt., 1991, Ser. [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]

Voss and Sloan, 1989
Voss, S.F.; Sloan, E.D., Thermal conductivity and heat capacity of synthetic fuel components, Int. J. Thermophys., 1989, 10(5), 1029-1040. [all data]

Saito and Tanaka, 1988
Saito, A.; Tanaka, R., Excess volumes and heat capacities of binary mixtures formed from cyclohexane, hexane and heptane at 298.15 K, J. Chem. Thermodynam., 1988, 20, 859-865. [all data]

Shiohama, Ogawa, et al., 1988
Shiohama, Y.; Ogawa, H.; Murakami, S.; Fujihara, I., Excess thermodynamic properties of (cis-decalin or trans-decalin + cyclohexane or methylcyclohexane or cyclooctane) at 298.15 K, J. Chem. Thermodynam., 1988, 20, 1307-1314. [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]

Jimenez, Romani, et al., 1986
Jimenez, E.; Romani, L.; Paz Andrade, M.I.; Roux-Desgranges, G.; Grolier, J.-P.E., Molar excess heat capacities and volumes for mixtures of alkanoates with cyclohexane at 25°C, J. Solution Chem., 1986, 15(11), 879-890. [all data]

Ortega, 1986
Ortega, J., Excess molar heat capacities of the binary mixtures of cyclohexane with isomers of hexanol at 298.15 K, Rev. Latinoam. Ing. Quim. Quim. Apl., 1986, 16, 307-315. [all data]

Nkinamubanzi, Charlet, et al., 1985
Nkinamubanzi, P.; Charlet, G.; Delmas, G., Excess enthalpies, excess heat capacities and excess volumes of tetraalkoxysilanes with cyclohexane and carbon tetrachloride, Fluid Phase Equilibria, 1985, 20, 57-73. [all data]

Tanaka, Nakamichi, et al., 1985
Tanaka, R.; Nakamichi, T.; Murakami, S., Molar excess heat capacities and volumes for mixtures of benzomitrile with cyclohexane between 10 and 45°C, J. Solution Chem., 1985, 14(11), 795-803. [all data]

Siddiqi, Svejda, et al., 1983
Siddiqi, M.A.; Svejda, P.; Kohler, F., A generalized van der Waals equation of state II. Excess heat capacities of mixtures containing cycloalkanes (C5,C6), methylcycloalkanes (C5,C6) and n-decane, Ber. Bunsenges. Phys. Chem., 1983, 87, 1176-1181. [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]

Fortier, D'Arcy, et al., 1979
Fortier, J.-L.; D'Arcy, P.J.; Benson, G.C., Heat capacities of binary cycloalkane mixtures at 298.15 K, Thermochim. Acta, 1979, 28, 37-43. [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]

Wilhelm, Grolier, et al., 1979
Wilhelm, E.; Grolier, G.-P.E.; Karbalai Ghassemi, M.H., Molar heat capacity of binary liquid mixtures: 1,2-dichloroethane + cyclohexane and 1,2-dichloroethane + methylcyclohexane, Thermochim. Acta, 1979, 28, 59-69. [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]

Safir, 1978
Safir, L.I., Experimental determination of the isobaric heat capacity of cyclohexane at atmospheric pressure, Izv. Vyssh. Uchebn. Zaved. Neft. Gaz 21, 1978, (12), 81-82. [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]

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]

Jolicoeur, Boileau, et al., 1975
Jolicoeur, C.; Boileau, J.; Bazinet, S.; Picker, P., Thermodynamic properties of aqueous organic solutes in relation to their structure. Part II. Apparent molal volumes and heat capacities of c-alkylamine hydrobromides in water, Can. J. Chem., 1975, 53, 716-722. [all data]

Wilhelm, Zettler, et al., 1974
Wilhelm, E.; Zettler, M.; Sackmann, H., Molar heat capacities for the binary systems cyclohexane, carbon tetrachloride, silicon tetrachloride and tin tetrachloride Ber. Bunsenges. Phys. Chem., 1974, 78, 795-804. [all data]

Subrahmanyam and Rajagopal, 1973
Subrahmanyam, S.V.; Rajagopal, E., Excess thermodynamic functions of the systems isooctane + carbon tetrachloride and isooctane + cyclohexane, Z. Phys. Chem. [NF], 1973, 85, 256-268. [all data]

Wilhelm, Schano, et al., 1969
Wilhelm, E.; Schano, R.; Becker, G.; Findenegg, G.H.; Kohler, F., Molar heat capacity at constant volume. Binary mixtures of 1,2-dichloroethane and 1,2-dibromoethane with cyclohexane, Trans. Faraday Soc., 1969, 65, 1443-1455. [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]

Nikolaev, Rabinovich, et al., 1966
Nikolaev, P.N.; Rabinovich, I.B.; Gal'perin, V.A.; Tsvetkov, V.G., Isotopic effect on the specific heat and compressibility of deuterocyclohexane, Zhur. Fiz. Khim., 1966, 40, 1091-1097. [all data]

Moelwyn-Hughes and Thorpe, 1964
Moelwyn-Hughes, E.A.; Thorpe, P.L., The physical and thermodynamic properties of some associated solutions. II. Heat capacities and compressibilities, Proc. Roy. Soc. (London), 1964, 278A, 574-587. [all data]

Swietoslawski and Zielenkiewicz, 1960
Swietoslawski, W.; Zielenkiewicz, A., Mean specific heat in homologous series of binary and ternary positive azeotropes, Bull. Acad. Pol. Sci. Ser. Sci. Chim., 1960, 8, 651-653. [all data]

Auerbach, Sage, et al., 1950
Auerbach, C.E.; Sage, B.H.; Lacey, W.N., Isobaric heat capacities at bubble point, Ind. Eng. Chem., 1950, 42, 110-113. [all data]

Phillip, 1939
Phillip, N.M., Adiabatic and isothermal compressibilities of liquids, Proc. Indian Acad. Sci., 1939, A9, 109-120. [all data]

Dejardin, 1919
Dejardin, G., Pressions maxima des vapeurs du benzene et du cyclohexane aux temperatures moyennes et calcul de leurs chaleurs specifiques principales, Ann. phys. [9], 1919, 11, 253-291. [all data]

Daubert, 1996
Daubert, T.E., Vapor-Liquid Critical Properties of Elements and Compounds. 5. Branched Alkanes and Cycloalkanes, J. Chem. Eng. Data, 1996, 41, 365-372. [all data]

Young, 1972
Young, C.L., Gas-liquid critical properties of the cycloalkanes and their mixtures, Aust. J. Chem., 1972, 25, 1625-30. [all data]

Teja and Anselme, 1990
Teja, A.S.; Anselme, M.J., The critical properties of thermally stable and unstable fluids. II. 1986 results, AIChE Symp. Ser., 1990, 86, 279, 122-7. [all data]

Simon, 1957
Simon, M., Methods and Apparatus Used at the Bureau of Physicochemical Standards XV. Critical Constants and Straight-Line Diameters of Ten Hydrocarbons, Bull. Soc. Chim. Belg., 1957, 66, 375-81. [all data]

Young, 1910
Young, S., The Internal Heat of Vaporization constants of thirty pure substances, Sci. Proc. R. Dublin Soc., 1910, 12, 374. [all data]

Young and Fortey, 1899
Young, S.; Fortey, E.C., The Vapour Pressures, Specific Volumes and Critical Constants of Hexamethylene., J. Chem. Soc., Trans., 1899, 75, 873. [all data]

Majer and Svoboda, 1985
Majer, V.; Svoboda, V., Enthalpies of Vaporization of Organic Compounds: A Critical Review and Data Compilation, Blackwell Scientific Publications, Oxford, 1985, 300. [all data]

Gierycz, Kosowski, et al., 2009
Gierycz, Pawel; Kosowski, Andrzej; Swietlik, Ryszard, Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols, J. Chem. Eng. Data, 2009, 54, 11, 2996-3001, https://doi.org/10.1021/je900050z . [all data]

Lubomska, Banas, et al., 2002
Lubomska, Monika; Banas, Agnieszka; Malanowski, Stanislaw K., Vapor-Liquid Equilibrium in Binary Systems Formed by Allyl Alcohol with Benzene and with Cyclohexane, J. Chem. Eng. Data, 2002, 47, 6, 1466-1471, https://doi.org/10.1021/je025540l . [all data]

Diogo, Santos, et al., 1995
Diogo, Hermínio P.; Santos, Rui C.; Nunes, Paulo M.; Minas da Piedade, Manuel E., Ebulliometric apparatus for the measurement of enthalpies of vaporization, Thermochimica Acta, 1995, 249, 113-120, https://doi.org/10.1016/0040-6031(95)90678-9 . [all data]

Lee and Holder, 1993
Lee, Chang Ha; Holder, Gerald D., Vapor-liquid equilibria in the systems toluene/naphthalene and cyclohexane/naphthalene, J. Chem. Eng. Data, 1993, 38, 2, 320-323, https://doi.org/10.1021/je00010a034 . [all data]

Dong, Lin, et al., 1988
Dong, Jin-Quan; Lin, Rui-Sen; Yen, Wen-Hsing, Heats of vaporization and gaseous molar heat capacities of ethanol and the binary mixture of ethanol and benzene, Can. J. Chem., 1988, 66, 4, 783-790, https://doi.org/10.1139/v88-136 . [all data]

Stephenson and Malanowski, 1987
Stephenson, Richard M.; Malanowski, Stanislaw, Handbook of the Thermodynamics of Organic Compounds, 1987, https://doi.org/10.1007/978-94-009-3173-2 . [all data]

Willingham, Taylor, et al., 1945
Willingham, C.B.; Taylor, W.J.; Pignocco, J.M.; Rossini, F.D., Vapor pressures and boiling points of some paraffin, alkylcyclopentane, alkylcyclohexane, and alkylbenzene hydrocarbons, J. RES. NATL. BUR. STAN., 1945, 35, 3, 219-17, https://doi.org/10.6028/jres.035.009 . [all data]

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Notes

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