Toluene

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Gas phase thermochemistry data

Go To: Top, Condensed phase thermochemistry data, Reaction thermochemistry data, Henry's Law 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
Δfgas50.1 ± 1.1kJ/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
Δfgas50.00 ± 0.63kJ/molCcbProsen, Gilmont, et al., 1945Hf by Prosen, Johnson, et al., 1946; ALS
Δfgas48.0kJ/molN/ASchmidlin, 1906Value computed using ΔfHliquid° value of 10.0 kj/mol from Schmidlin, 1906 and ΔvapH° value of 38.0 kj/mol from Prosen, Gilmont, et al., 1945.; DRB

Constant pressure heat capacity of gas

Cp,gas (J/mol*K) Temperature (K) Reference Comment
69.85200.Draeger, 1985Recommended values agree better with experimental heat capacities than results of calculation [ Chao J., 1984]. All other statistically calculated values [ Pitzer K.S., 1943, Taylor W.J., 1946, Scott D.W., 1962] are in close agreement with selected ones, except for high temperatures.; GT
94.68273.15
103.7 ± 0.4298.15
104.4300.
139.9400.
170.8500.
196.2600.
217.0700.
234.3800.
248.9900.
261.21000.
271.81100.
280.81200.
288.51300.
295.21400.
301.01500.

Constant pressure heat capacity of gas

Cp,gas (J/mol*K) Temperature (K) Reference Comment
130.08 ± 0.26371.20Scott D.W., 1962Please also see Montgomery J.B., 1942, Pitzer K.S., 1943, Taylor W.J., 1946.; GT
140.2390.
137.2 ± 1.3393.
138.87 ± 0.27396.20
146.4410.
149.16 ± 0.30427.20
149.4 ± 1.7428.
160.33 ± 0.32462.20
159.0 ± 1.7463.
171.46 ± 0.34500.20

Condensed phase thermochemistry data

Go To: Top, Gas phase thermochemistry data, Reaction thermochemistry data, Henry's Law 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. ± 1.1kJ/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
Δfliquid12.0 ± 0.63kJ/molCcbProsen, Gilmont, et al., 1945Hf by Prosen, Johnson, et al., 1946; ALS
Δfliquid  CcbSchmidlin, 1906uncertain value: 10. kJ/mol; Undetermine error; ALS
Quantity Value Units Method Reference Comment
Δcliquid-3920. ± 20.kJ/molAVGN/AAverage of 5 out of 6 values; Individual data points
Quantity Value Units Method Reference Comment
liquid220.96J/mol*KN/AScott, Guthrie, et al., 1962DH
liquid219.2J/mol*KN/AKelley, 1929DH

Constant pressure heat capacity of liquid

Cp,liquid (J/mol*K) Temperature (K) Reference Comment
157.09298.15Grolier, Roux-Desgranges, et al., 1993DH
155.96298.15Shiohama, Ogawa, et al., 1988DH
159.9303.15Reddy, 1986T = 303.15, 313.15 K.; DH
157.08298.15Roux-Dexgranges, Grolier, et al., 1986DH
158.70298.15Tardajos, Aicart, et al., 1986DH
158.7298.15Stephens and Olson, 1984T = 266 to 318 K. Cp given as 0.4117 cal g-1 C-1.; DH
157.0298.15Grolier, Inglese, et al., 1982DH
157.15298.15Wilhelm, Faradjzadeh, et al., 1982DH
156.0293.15Atalla, El-Sharkawy, et al., 1981DH
157.0294.71Andolenko and Grigor'ev, 1979T = 293 to 373 K. Unsoothed experimental datum given as 1.704 KJ/kg*K.; DH
157.057298.15Fortier and Benson, 1979DH
157.081298.15Fortier and Benson, 1977DH
156.94298.15Wilhelm, Grolier, et al., 1977DH
157.026298.15Fortier and Benson, 1976DH
156.99298.15Holzhauer and Ziegler, 1975T = 165 to 312 K. Cp = 187.43814 - 0.73026493T + 0.0029613602T2 - 2.8661704x10-6T3 J/mol*K.; DH
158.4298.15Pedersen, Kay, et al., 1975T = 298 to 348 K. Cp(liq) = 154.73 + 0.0981(T/K-273.15) + 0.001949(T/K-273.15)2 J/mol*K (298 to 348 K).; DH
156.8298.15Rajagopal and Subrahmanyam, 1974T = 298.15 to 323.15 K.; DH
156.5298.Deshpande and Bhatagadde, 1971T = 298 to 318 K.; DH
158.6293.Rastorguev and Ganiev, 1967T = 293 to 373 K.; DH
157.33298.711Hwa and Ziegler, 1966T = 181 to 304 K. Unsmoothed experimental datum.; DH
157.23298.15Scott, Guthrie, et al., 1962T = 10 to 360 K.; DH
166.9324.Swietoslawski and Zielenkiewicz, 1958Mean value 21 to 81 C.; DH
140.295.Tschamler, 1948DH
158.6298.Kurbatov, 1947T = -76 to 60 C, mean Cp, four temperatures.; DH
156.9298.1Zhdanov, 1941T = 5 to 47 C.; DH
157.07298.2Burlew, 1940T = 281 to 383 K.; DH
156.5298.Vold, 1937DH
142.7227.8Aoyama and Kanda, 1935T = 78 to 228 K. Value is unsmoothed experimental datum.; DH
156.5298.1Richards and Wallace, 1932T = 293 to 333 K.; DH
161.9298.15Smith and Andrews, 1931T = 102 to 299 K. Value is unsmoothed experimental datum.; DH
153.0928.444Kelley, 1929T = 14 to 284 K. Value is unsmoothed experimental datum.; DH
151.0293.2Williams and Daniels, 1925T = 20 to 60 C.; DH
153.6303.Willams and Daniels, 1924T = 303 to 343 K. Equation only.; DH
158.2298.von Reis, 1881T = 292 to 390 K.; DH

Reaction thermochemistry data

Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Henry's Law 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:
B - John E. Bartmess
M - Michael M. Meot-Ner (Mautner) and Sharon G. Lias
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
RCD - Robert C. Dunbar

Note: Please consider using the reaction search for this species. This page allows searching of all reactions involving this species. A general reaction search form is also available. Future versions of this site may rely on reaction search pages in place of the enumerated reaction displays seen below.

Individual Reactions

C7H7- + Hydrogen cation = Toluene

By formula: C7H7- + H+ = C7H8

Quantity Value Units Method Reference Comment
Δr1599.7 ± 1.9kJ/molD-EAGunion, Gilles, et al., 1992gas phase; Kim, Wenthold, et al., 1999, with LN2 cooling of the ion, gives the same EA; B
Δr1593. ± 8.8kJ/molG+TSBartmess, Scott, et al., 1979gas phase; value altered from reference due to change in acidity scale; B
Δr1587. ± 8.8kJ/molG+TSGal, Decouzon, et al., 2001gas phase; B
Δr1577. ± 15.kJ/molCIDTGraul and Squires, 1990gas phase; B
Δr1609. ± 30.kJ/molG+TSBohme and Young, 1971gas phase; B
Quantity Value Units Method Reference Comment
Δr1564. ± 8.4kJ/molIMREBartmess, Scott, et al., 1979gas phase; value altered from reference due to change in acidity scale; B
Δr1557. ± 8.4kJ/molIMREGal, Decouzon, et al., 2001gas phase; B
Δr1579. ± 29.kJ/molIMRBBohme and Young, 1971gas phase; B

C3H9Si+ + Toluene = (C3H9Si+ • Toluene)

By formula: C3H9Si+ + C7H8 = (C3H9Si+ • C7H8)

Quantity Value Units Method Reference Comment
Δr119.kJ/molPHPMSStone and Stone, 1991gas phase; forms pi complex; M
Δr131.kJ/molPHPMSStone and Stone, 1991gas phase; toluene D8, forms pi complex; M
Δr111.kJ/molPHPMSWojtyniak and Stone, 1986gas phase; switching reaction,Thermochemical ladder((CH3)3Si+)C6H6, Entropy change calculated or estimated; M
Quantity Value Units Method Reference Comment
Δr146.J/mol*KN/AWojtyniak and Stone, 1986gas phase; switching reaction,Thermochemical ladder((CH3)3Si+)C6H6, Entropy change calculated or estimated; M

Free energy of reaction

ΔrG° (kJ/mol) T (K) Method Reference Comment
43.1468.PHPMSWojtyniak and Stone, 1986gas phase; switching reaction,Thermochemical ladder((CH3)3Si+)C6H6, Entropy change calculated or estimated; M

Bromine anion + Toluene = (Bromine anion • Toluene)

By formula: Br- + C7H8 = (Br- • C7H8)

Quantity Value Units Method Reference Comment
Δr36. ± 7.5kJ/molIMREPaul and Kebarle, 1991gas phase; ΔGaff measured at 303 K, corrected to 423 K, ΔSaff taken as that of PhNO2..Br-; B,M
Quantity Value Units Method Reference Comment
Δr84.J/mol*KN/APaul and Kebarle, 1991gas phase; Entropy change calculated or estimated; M
Quantity Value Units Method Reference Comment
Δr0.4 ± 4.2kJ/molIMREPaul and Kebarle, 1991gas phase; ΔGaff measured at 303 K, corrected to 423 K, ΔSaff taken as that of PhNO2..Br-; B

Free energy of reaction

ΔrG° (kJ/mol) T (K) Method Reference Comment
0.4423.PHPMSPaul and Kebarle, 1991gas phase; Entropy change calculated or estimated; M

C4H9+ + Toluene = (C4H9+ • Toluene)

By formula: C4H9+ + C7H8 = (C4H9+ • C7H8)

Quantity Value Units Method Reference Comment
Δr120.kJ/molPHPMSStone and Stone, 1991gas phase; toluene D8, forms protonated t-butyltoluene; M
Δr122.kJ/molPHPMSStone and Stone, 1991gas phase; forms protomated t-butyltoluene; M
Quantity Value Units Method Reference Comment
Δr228.J/mol*KPHPMSStone and Stone, 1991gas phase; toluene D8, forms protonated t-butyltoluene; M
Δr228.J/mol*KPHPMSStone and Stone, 1991gas phase; forms protomated t-butyltoluene; M

C7H8+ + Toluene = (C7H8+ • Toluene)

By formula: C7H8+ + C7H8 = (C7H8+ • C7H8)

Bond type: Charge transfer bond (positive ion)

Quantity Value Units Method Reference Comment
Δr60.7kJ/molMPIErnstberger, Krause, et al., 1990gas phase; M
Δr23.kJ/molPIRuhl, Bisling, et al., 1986gas phase; from vIP of perpendicular dimer; M
Δr66.9kJ/molPHPMSMeot-Ner (Mautner), Hamlet, et al., 1978gas phase; M
Quantity Value Units Method Reference Comment
Δr120.J/mol*KPHPMSMeot-Ner (Mautner), Hamlet, et al., 1978gas phase; M

C6H7N+ + Toluene = (C6H7N+ • Toluene)

By formula: C6H7N+ + C7H8 = (C6H7N+ • C7H8)

Bond type: Charge transfer bond (positive ion)

Quantity Value Units Method Reference Comment
Δr57.3kJ/molPHPMSMeot-Ner (Mautner) and El-Shall, 1986gas phase; M
Quantity Value Units Method Reference Comment
Δr109.J/mol*KPHPMSMeot-Ner (Mautner) and El-Shall, 1986gas phase; M

C9H12+ + Toluene = (C9H12+ • Toluene)

By formula: C9H12+ + C7H8 = (C9H12+ • C7H8)

Bond type: Charge transfer bond (positive ion)

Quantity Value Units Method Reference Comment
Δr50.2kJ/molPHPMSMeot-Ner (Mautner), Hamlet, et al., 1978gas phase; M
Quantity Value Units Method Reference Comment
Δr110.J/mol*KPHPMSMeot-Ner (Mautner), Hamlet, et al., 1978gas phase; M

Nitric oxide anion + Toluene = (Nitric oxide anion • Toluene)

By formula: NO- + C7H8 = (NO- • C7H8)

Quantity Value Units Method Reference Comment
Δr185.kJ/molICRReents and Freiser, 1981gas phase; switching reaction,Thermochemical ladder(NO+)C2H5OH, Entropy change calculated or estimated; Farid and McMahon, 1978; M

Hydrogen bromide + Benzene, (bromomethyl)- = Toluene + Bromine

By formula: HBr + C7H7Br = C7H8 + Br2

Quantity Value Units Method Reference Comment
Δr33.9 ± 4.2kJ/molEqkBenson and Buss, 1957gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = 33. ± 4. kJ/mol; ALS

Chlorine anion + Toluene = (Chlorine anion • Toluene)

By formula: Cl- + C7H8 = (Cl- • C7H8)

Quantity Value Units Method Reference Comment
Δr16.7kJ/molTDEqFrench, Ikuta, et al., 1982gas phase; B

Free energy of reaction

ΔrG° (kJ/mol) T (K) Method Reference Comment
17.300.PHPMSFrench, Ikuta, et al., 1982gas phase; M

Hydrogen iodide + Benzene, (iodomethyl)- = Toluene + Iodine

By formula: HI + C7H7I = C7H8 + I2

Quantity Value Units Method Reference Comment
Δr-33. ± 4.6kJ/molCmGraham, Nichol, et al., 1955liquid phase; solvent: p-Xylene; ALS

Benzene, (bromomethyl)- + 0.5Hydrogen = Toluene + 0.5Bromine

By formula: C7H7Br + 0.5H2 = C7H8 + 0.5Br2

Quantity Value Units Method Reference Comment
Δr-4. ± 2.kJ/molChydAshcroft, Carson, et al., 1963liquid phase; ALS

Iodide + Toluene = (Iodide • Toluene)

By formula: I- + C7H8 = (I- • C7H8)

Quantity Value Units Method Reference Comment
Δr46.0 ± 4.2kJ/molTDAsCaldwell, Masucci, et al., 1989gas phase; B,M

5-Methylene 1,3-cyclohexadiene = Toluene

By formula: C7H8 = C7H8

Quantity Value Units Method Reference Comment
Δr-100. ± 10.kJ/molCmBartmess and Griffith, 1990gas phase; Gas phase acidity; ALS

Benzene, (iodomethyl)- = Toluene + 0.5Iodine

By formula: C7H7I = C7H8 + 0.5I2

Quantity Value Units Method Reference Comment
Δr-41. ± 2.kJ/molChydAshcroft, Carson, et al., 1963liquid phase; ALS

(Lithium ion (1+) • Toluene) + Toluene = (Lithium ion (1+) • 2Toluene)

By formula: (Li+ • C7H8) + C7H8 = (Li+ • 2C7H8)

Quantity Value Units Method Reference Comment
Δr116. ± 3.kJ/molCIDTAmunugama and Rodgers, 2002RCD

(Sodium ion (1+) • Toluene) + Toluene = (Sodium ion (1+) • 2Toluene)

By formula: (Na+ • C7H8) + C7H8 = (Na+ • 2C7H8)

Quantity Value Units Method Reference Comment
Δr87. ± 2.kJ/molCIDTAmunugama and Rodgers, 2002RCD

(Cesium ion (1+) • Toluene) + Toluene = (Cesium ion (1+) • 2Toluene)

By formula: (Cs+ • C7H8) + C7H8 = (Cs+ • 2C7H8)

Quantity Value Units Method Reference Comment
Δr61.5 ± 4.2kJ/molCIDTAmunugama and Rodgers, 2002RCD

(Rubidium ion (1+) • Toluene) + Toluene = (Rubidium ion (1+) • 2Toluene)

By formula: (Rb+ • C7H8) + C7H8 = (Rb+ • 2C7H8)

Quantity Value Units Method Reference Comment
Δr67.8 ± 4.2kJ/molCIDTAmunugama and Rodgers, 2002RCD

(Potassium ion (1+) • Toluene) + Toluene = (Potassium ion (1+) • 2Toluene)

By formula: (K+ • C7H8) + C7H8 = (K+ • 2C7H8)

Quantity Value Units Method Reference Comment
Δr74.9 ± 4.6kJ/molCIDTAmunugama and Rodgers, 2002RCD

(Chromium ion (1+) • Toluene) + Toluene = (Chromium ion (1+) • 2Toluene)

By formula: (Cr+ • C7H8) + C7H8 = (Cr+ • 2C7H8)

Quantity Value Units Method Reference Comment
Δr222. ± 38.kJ/molRAKLin and Dunbar, 1997RCD

Benzene, 1-methyl-3-(1-methylethyl)- + Benzene = Toluene + Benzene, (1-methylethyl)-

By formula: C10H14 + C6H6 = C7H8 + C9H12

Quantity Value Units Method Reference Comment
Δr0.0 ± 0.6kJ/molEqkTsvetkov, Rozhnov, et al., 1985liquid phase; ALS

Lithium ion (1+) + Toluene = (Lithium ion (1+) • Toluene)

By formula: Li+ + C7H8 = (Li+ • C7H8)

Quantity Value Units Method Reference Comment
Δr183. ± 17.kJ/molCIDTAmunugama and Rodgers, 2002RCD

Sodium ion (1+) + Toluene = (Sodium ion (1+) • Toluene)

By formula: Na+ + C7H8 = (Na+ • C7H8)

Quantity Value Units Method Reference Comment
Δr112. ± 3.kJ/molCIDTAmunugama and Rodgers, 2002RCD

Cesium ion (1+) + Toluene = (Cesium ion (1+) • Toluene)

By formula: Cs+ + C7H8 = (Cs+ • C7H8)

Quantity Value Units Method Reference Comment
Δr64.0 ± 4.6kJ/molCIDTAmunugama and Rodgers, 2002RCD

Rubidium ion (1+) + Toluene = (Rubidium ion (1+) • Toluene)

By formula: Rb+ + C7H8 = (Rb+ • C7H8)

Quantity Value Units Method Reference Comment
Δr71.1 ± 4.2kJ/molCIDTAmunugama and Rodgers, 2002RCD

Potassium ion (1+) + Toluene = (Potassium ion (1+) • Toluene)

By formula: K+ + C7H8 = (K+ • C7H8)

Quantity Value Units Method Reference Comment
Δr79.9 ± 5.0kJ/molCIDTAmunugama and Rodgers, 2002RCD

Chromium ion (1+) + Toluene = (Chromium ion (1+) • Toluene)

By formula: Cr+ + C7H8 = (Cr+ • C7H8)

Quantity Value Units Method Reference Comment
Δr176. ± 14.kJ/molRAKLin and Dunbar, 1997RCD

Henry's Law data

Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Reaction 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 by: Rolf Sander

Henry's Law constant (water solution)

kH(T) = H exp(d(ln(kH))/d(1/T) ((1/T) - 1/(298.15 K)))
H = Henry's law constant for solubility in water at 298.15 K (mol/(kg*bar))
d(ln(kH))/d(1/T) = Temperature dependence constant (K)

H (mol/(kg*bar)) d(ln(kH))/d(1/T) (K) Method Reference Comment
0.154000.LN/A 
0.184100.MN/A 
0.16 MN/A 
0.16 XN/AValue given here as cited in missing citation.
0.13 MN/A 
0.153400.MN/A 
0.16 XN/AValue given here as cited in missing citation.
0.16 QN/A missing citation give several references for the Henry's law constants but don't assign them to specific species.
0.145000.XN/A 
0.178400.XN/A 
0.153000.XN/A 
0.151900.XN/A 
0.153700.XLeighton and Calo, 1981 
0.15 LN/A 
0.154900.XN/A 
0.15 MMackay, Shiu, et al., 1979 
0.15 TMackay, Shiu, et al., 1979 
0.15 VN/A 
0.19 MN/A 
0.214600.MN/A 
0.15 XN/AValue given here as cited in missing citation.
0.175900.MN/A 
0.18 VBohon and Claussen, 1951 

References

Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Reaction thermochemistry data, Henry's Law 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]

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]

Schmidlin, 1906
Schmidlin, M.J., Recherches chimiques et thermochimiques sur la constitution des rosanilines, Ann. Chim. Phys., 1906, 1, 195-256. [all data]

Draeger, 1985
Draeger, J.A., The methylbenzenes II. Fundamental vibrational shifts, statistical thermodynamic functions, and properties of formation, J. Chem. Thermodyn., 1985, 17, 263-275. [all data]

Chao J., 1984
Chao J., Chemical thermodynamic properties of toluene, o-, m- and p-xylenes, Thermochim. Acta, 1984, 72, 323-334. [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]

Taylor W.J., 1946
Taylor W.J., Heats, equilibrium constants, and free energies of formation of the alkylbenzenes, J. Res. Nat. Bur. Stand., 1946, 37, 95-122. [all data]

Scott D.W., 1962
Scott D.W., Toluene: thermodynamic properties, molecular vibrations, and internal rotation, J. Phys. Chem., 1962, 66, 911-914. [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]

Scott, Guthrie, et al., 1962
Scott, D.W.; Guthrie, G.B.; Messerly, J.F.; Todd, S.S.; Berg, W.T.; Hossenlopp, I.A.; McCullough, J.P., Toluene: thermodynamic properties, molecular vibrations, and internal rotation, J. Phys. Chem., 1962, 66, 911-914. [all data]

Kelley, 1929
Kelley, K.K., The heat capacity of toluene from 14K to 298K. The entropy and the free energy of formation, J. Am. Chem. Soc., 1929, 51, 2738-2741. [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]

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]

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]

Roux-Dexgranges, Grolier, et al., 1986
Roux-Dexgranges, G.; Grolier, J.-P.E.; Villamanan, M.A.; Casanova, C., Role of alcohol in microemulsions. III. Volumes and heat capacities in the continuious phase water-n-butanol-toluene of reverse micelles, Fluid Phase Equilibria, 1986, 25, 209-230. [all data]

Tardajos, Aicart, et al., 1986
Tardajos, G.; Aicart, E.; Costas, M.; Patterson, D., Liquid structure and second-order mixing functions for benzene, toluene, and p-xylene with n-alkanes, J. Chem. Soc., Faraday Trans., 1986, 1 82, 2977-2987. [all data]

Stephens and Olson, 1984
Stephens, M.; Olson, J.D., Measurement of excess heat capacities by differential scanning calorimetry, Thermochim. Acta, 1984, 76, 79-85. [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]

Wilhelm, Faradjzadeh, et al., 1982
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Notes

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