Toluene
- Formula: C7H8
- Molecular weight: 92.1384
- IUPAC Standard InChIKey: YXFVVABEGXRONW-UHFFFAOYSA-N
- CAS Registry Number: 108-88-3
- 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: Benzene, methyl; Methacide; Methylbenzene; Methylbenzol; Phenylmethane; Antisal 1a; Toluol; Methane, phenyl-; NCI-C07272; Tolueen; Toluen; Toluolo; Rcra waste number U220; Tolu-sol; UN 1294; Dracyl; Monomethyl benzene; CP 25; NSC 406333; methylbenzene (toluene)
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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 | 12. ± 1.1 | 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 | 12.0 ± 0.63 | kJ/mol | Ccb | Prosen, Gilmont, et al., 1945 | Hf by Prosen, Johnson, et al., 1946; ALS |
ΔfH°liquid | Ccb | Schmidlin, 1906 | uncertain value: 10. kJ/mol; Undetermine error; ALS | ||
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -3920. ± 20. | kJ/mol | AVG | N/A | Average of 5 out of 6 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
S°liquid | 220.96 | J/mol*K | N/A | Scott, Guthrie, et al., 1962 | DH |
S°liquid | 219.2 | J/mol*K | N/A | Kelley, 1929 | DH |
Constant pressure heat capacity of liquid
Cp,liquid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
157.09 | 298.15 | Grolier, Roux-Desgranges, et al., 1993 | DH |
155.96 | 298.15 | Shiohama, Ogawa, et al., 1988 | DH |
159.9 | 303.15 | Reddy, 1986 | T = 303.15, 313.15 K.; DH |
157.08 | 298.15 | Roux-Dexgranges, Grolier, et al., 1986 | DH |
158.70 | 298.15 | Tardajos, Aicart, et al., 1986 | DH |
158.7 | 298.15 | Stephens and Olson, 1984 | T = 266 to 318 K. Cp given as 0.4117 cal g-1 C-1.; DH |
157.0 | 298.15 | Grolier, Inglese, et al., 1982 | DH |
157.15 | 298.15 | Wilhelm, Faradjzadeh, et al., 1982 | DH |
156.0 | 293.15 | Atalla, El-Sharkawy, et al., 1981 | DH |
157.0 | 294.71 | Andolenko and Grigor'ev, 1979 | T = 293 to 373 K. Unsoothed experimental datum given as 1.704 KJ/kg*K.; DH |
157.057 | 298.15 | Fortier and Benson, 1979 | DH |
157.081 | 298.15 | Fortier and Benson, 1977 | DH |
156.94 | 298.15 | Wilhelm, Grolier, et al., 1977 | DH |
157.026 | 298.15 | Fortier and Benson, 1976 | DH |
156.99 | 298.15 | Holzhauer and Ziegler, 1975 | T = 165 to 312 K. Cp = 187.43814 - 0.73026493T + 0.0029613602T2 - 2.8661704x10-6T3 J/mol*K.; DH |
158.4 | 298.15 | Pedersen, Kay, et al., 1975 | T = 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 |
156.8 | 298.15 | Rajagopal and Subrahmanyam, 1974 | T = 298.15 to 323.15 K.; DH |
156.5 | 298. | Deshpande and Bhatagadde, 1971 | T = 298 to 318 K.; DH |
158.6 | 293. | Rastorguev and Ganiev, 1967 | T = 293 to 373 K.; DH |
157.33 | 298.711 | Hwa and Ziegler, 1966 | T = 181 to 304 K. Unsmoothed experimental datum.; DH |
157.23 | 298.15 | Scott, Guthrie, et al., 1962 | T = 10 to 360 K.; DH |
166.9 | 324. | Swietoslawski and Zielenkiewicz, 1958 | Mean value 21 to 81 C.; DH |
140. | 295. | Tschamler, 1948 | DH |
158.6 | 298. | Kurbatov, 1947 | T = -76 to 60 C, mean Cp, four temperatures.; DH |
156.9 | 298.1 | Zhdanov, 1941 | T = 5 to 47 C.; DH |
157.07 | 298.2 | Burlew, 1940 | T = 281 to 383 K.; DH |
156.5 | 298. | Vold, 1937 | DH |
142.7 | 227.8 | Aoyama and Kanda, 1935 | T = 78 to 228 K. Value is unsmoothed experimental datum.; DH |
156.5 | 298.1 | Richards and Wallace, 1932 | T = 293 to 333 K.; DH |
161.9 | 298.15 | Smith and Andrews, 1931 | T = 102 to 299 K. Value is unsmoothed experimental datum.; DH |
153.09 | 28.444 | Kelley, 1929 | T = 14 to 284 K. Value is unsmoothed experimental datum.; DH |
151.0 | 293.2 | Williams and Daniels, 1925 | T = 20 to 60 C.; DH |
153.6 | 303. | Willams and Daniels, 1924 | T = 303 to 343 K. Equation only.; DH |
158.2 | 298. | von Reis, 1881 | T = 292 to 390 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
DH - Eugene S. Domalski and Elizabeth D. Hearing
DRB - Donald R. Burgess, Jr.
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
AC - William E. Acree, Jr., James S. Chickos
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 383.8 ± 0.2 | K | AVG | N/A | Average of 110 out of 132 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 178.1 ± 0.6 | K | AVG | N/A | Average of 24 out of 25 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 178.15 | K | N/A | Scott, Guthrie, et al., 1962, 2 | Uncertainty assigned by TRC = 0.05 K; TRC |
Ttriple | 178.00 | K | N/A | Ziegler and Andrews, 1942 | Uncertainty assigned by TRC = 0.2 K; TRC |
Ttriple | 177.9 | K | N/A | Stull, 1937 | Uncertainty assigned by TRC = 0.2 K; TRC |
Ttriple | 177.95 | K | N/A | Kelley, 1929, 2 | Uncertainty assigned by TRC = 0.02 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 593. ± 2. | K | AVG | N/A | Average of 20 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 41. ± 1. | bar | AVG | N/A | Average of 11 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Vc | 0.316 | l/mol | N/A | Tsonopoulos and Ambrose, 1995 | |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 3.17 ± 0.010 | mol/l | N/A | Tsonopoulos and Ambrose, 1995 | |
ρc | 3.16 | mol/l | N/A | Chirico and Steele, 1994 | Uncertainty assigned by TRC = 0.04 mol/l; TRC |
ρc | 3.15 | mol/l | N/A | Goodwin, 1989 | Uncertainty assigned by TRC = 0.05 mol/l; TRC |
ρc | 3.16 | mol/l | N/A | Steele, Chirico, et al., 1988 | Uncertainty assigned by TRC = 0.05 mol/l; TRC |
ρc | 3.162 | mol/l | N/A | Simon, 1957 | Uncertainty assigned by TRC = 0.05 mol/l; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 37. ± 3. | kJ/mol | AVG | N/A | Average of 9 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ΔsubH° | 43.1 | kJ/mol | B | Lenchitz and Velicky, 1970 | AC |
Reduced pressure boiling point
Tboil (K) | Pressure (bar) | Reference | Comment |
---|---|---|---|
287.7 | 0.020 | Weast and Grasselli, 1989 | BS |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
33.18 | 383.8 | N/A | Majer and Svoboda, 1985 | |
35.7 | 346. | N/A | Lee and Holder, 1993 | Based on data from 331. to 496. K.; AC |
40.6 | 264. | A | Stephenson and Malanowski, 1987 | Based on data from 210. to 279. K.; AC |
34.4 | 398. | A | Stephenson and Malanowski, 1987 | Based on data from 383. to 445. K.; AC |
33.2 | 455. | A | Stephenson and Malanowski, 1987 | Based on data from 440. to 531. K.; AC |
33.3 | 545. | A | Stephenson and Malanowski, 1987 | Based on data from 530. to 592. K.; AC |
38.9 | 284. | A | Stephenson and Malanowski, 1987 | Based on data from 273. to 295. K.; AC |
37.0 | 323. | N/A | Stephenson and Malanowski, 1987 | Based on data from 308. to 386. K. See also Forziati, Norris, et al., 1949.; AC |
33.5 ± 0.1 | 380. | C | Natarajan and Viswanath, 1985 | AC |
32.1 ± 0.1 | 403. | C | Natarajan and Viswanath, 1985 | AC |
29.4 ± 0.1 | 441. | C | Natarajan and Viswanath, 1985 | AC |
27.1 ± 0.1 | 470. | C | Natarajan and Viswanath, 1985 | AC |
24.0 ± 0.1 | 505. | C | Natarajan and Viswanath, 1985 | AC |
35.4 | 333. | N/A | Eubank, Cediel, et al., 1984 | AC |
33.4 | 373. | N/A | Eubank, Cediel, et al., 1984 | AC |
31.4 | 413. | N/A | Eubank, Cediel, et al., 1984 | AC |
28.4 | 453. | N/A | Eubank, Cediel, et al., 1984 | AC |
24.0 | 493. | N/A | Eubank, Cediel, et al., 1984 | AC |
35.4 | 360. | N/A | Rivenq, 1975 | Based on data from 343. to 383. K.; AC |
37.3 | 318. | N/A | Gaw and Swinton, 1968 | Based on data from 303. to 343. K.; AC |
36.9 | 303. | N/A | Van Ness, Soczek, et al., 1967 | Based on data from 288. to 348. K.; AC |
35.65 | 341.27 | V | Scott, Gutherie, et al., 1962 | low T and vapor flow calorimetry; ALS |
37.8 | 278. | N/A | Milazzo, 1956 | Based on data from 210. to 293. K.; AC |
37.8 | 301. | N/A | Thomson, 1946 | Based on data from 286. to 362. K.; AC |
37.0 | 323. | MM | Willingham, Taylor, et al., 1945 | Based on data from 308. to 384. K.; AC |
38.8 | 288. | N/A | Pitzer and Scott, 1943 | Based on data from 273. to 323. K.; AC |
Enthalpy of vaporization
ΔvapH =
A exp(-βTr) (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) | A (kJ/mol) | β | Tc (K) | Reference | Comment |
---|---|---|---|---|---|
298. to 410. | 53.09 | 0.2774 | 591.7 | 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 |
---|---|---|---|---|---|
273.13 to 297.89 | 4.23679 | 1426.448 | -45.957 | Besley and Bottomley, 1974 | Coefficents calculated by NIST from author's data. |
303. to 343. | 4.08245 | 1346.382 | -53.508 | Gaw and Swinton, 1968, 2 | Coefficents calculated by NIST from author's data. |
420.00 to 580.00 | 4.54436 | 1738.123 | 0.394 | Ambrose, Broderick, et al., 1967 | Coefficents calculated by NIST from author's data. |
308.52 to 384.66 | 4.07827 | 1343.943 | -53.773 | Williamham, Taylor, et al., 1945 | |
273. to 323. | 4.14157 | 1377.578 | -50.507 | Pitzer and Scott, 1943 | Coefficents calculated by NIST from author's data. |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
6.636 | 178.15 | Scott, Guthrie, et al., 1962 | DH |
6.619 | 177.95 | Kelley, 1929 | DH |
6.548 | 178.0 | Ziegler and Andrews, 1942, 2 | DH |
6.61 | 178. | Domalski and Hearing, 1996 | See also Southard and Andrews, 1930.; AC |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
37.25 | 178.15 | Scott, Guthrie, et al., 1962 | DH |
37.20 | 177.95 | Kelley, 1929 | DH |
36.79 | 178.0 | Ziegler and Andrews, 1942, 2 | 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,
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Heats of combustion of benzene, toluene, ethyl-benzene, o-xylene, m-xylene, p-xylene, n-propylbenzene, and styrene,
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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,
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Recherches chimiques et thermochimiques sur la constitution des rosanilines,
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Toluene: thermodynamic properties, molecular vibrations, and internal rotation,
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Kelley, 1929
Kelley, K.K.,
The heat capacity of toluene from 14K to 298K. The entropy and the free energy of formation,
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Grolier, Roux-Desgranges, et al., 1993
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Heat capacities and densities of mixtures of very polar substances 2. Mixtures containing N,N-dimethylformamide,
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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,
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Reddy, 1986
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Isentropic compressibilities of binary liquid mixtures at 303.15 and 313.15 K,
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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,
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Liquid structure and second-order mixing functions for benzene, toluene, and p-xylene with n-alkanes, J. Chem. Soc.,
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Measurement of excess heat capacities by differential scanning calorimetry,
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Excess volumes and excess heat capacities of tetrachloroethene + cyclohexane, + methylcyclohexane, + benzene, and + toluene at 298.15 K,
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Wilhelm, Faradjzadeh, et al., 1982
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Excess volumes and excess heat capacities of 2,3-dimethylbutane + butane and + toluene,
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Atalla, El-Sharkawy, et al., 1981
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Measurement of thermal properties of liquids with an AC heated-wire technique,
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Andolenko and Grigor'ev, 1979
Andolenko, R.A.; Grigor'ev, B.A.,
Investigation of isobaric heat capacity of aromatic hydrocarbons at atmospheric pressure, Iaz. Vyssh. Ucheb. Zaved.,
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Fortier and Benson, 1979
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Heat capacities of some binary aromatic hydrocarbon mixtures containing benzene or toluene,
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Fortier and Benson, 1977
Fortier, J.-L.; Benson, G.C.,
Excess heat capacities of binary mixtures of tetrachloromethane witlh some aromatic liquids at 298.15 K,
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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,
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Excess heat capacities of binary liquid mixtures determined with a Picker flow calorimeter,
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Holzhauer, J.K.; Ziegler, W.T.,
Temperature dependence of excess thermodynamic properties of n-heptane-toluene, methylcyclohexane-toluene, and n-heptane-methylcyclohexane systems,
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Excess enthalpies, heat capacities, and excess heat capacities as a function of temperature in liquid mixtures of ethanol + toluene, ethanol + hexamethyldisiloxane, and hexamethyldisiloxane + toluene,
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Rajagopal and Subrahmanyam, 1974
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Excess function of VE,(dVE/dp)T, and CpE of isooctane + benzene and + toluene,
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Heat capacities at constant volume, free volumes, and rotational freedom in some liquids,
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Rastorguev, Yu.L.; Ganiev, Yu.A.,
Study of the heat capacity of selected solvents,
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Hwa, S.C.P.; Ziegler, W.T.,
Temperature dependence of excess thermodynamic properties of ethanol-methylcyclohexane and ethanol-toluene systems,
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Mean specific heats of binary positive azeotropes,
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Tschamler, H.,
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Specific heat of liquids. I. Specific heat of benzenoid hydrocarbons,
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Specific heats of some liquids and azeotropic mixtures,
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Burlew, 1940
Burlew, J.S.,
Measurement of the heat capacity of a small volume of liquid by the piezo-thermometric method. III. Heat capacity of benzene and of toluene from 8°C. to the boiling point,
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Vold, 1937
Vold, R.D.,
A calorimetric test of the solubility equation for regular solutions,
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Aoyama and Kanda, 1935
Aoyama, S.; Kanda, E.,
Studies on the heat capacities at low temperature. Report I. Heat capacities of some organic substances at low temperature,
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The specific heats of five organic liquids from their adiabatic temperature-pressure coefficients,
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Smith, R.H.; Andrews, D.H.,
Thermal energy studies. I. Phenyl derivatives of methane,
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Williams, J.W.; Daniels, F.,
The specific heats of binary mixtures,
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Willams and Daniels, 1924
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The specific heats of certain organic liquids at elevated temperatures,
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von Reis, M.A.,
Die specifische Wärme flüssiger organischer Verbindungen und ihre Beziehung zu deren Moleculargewicht,
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Scott, D.W.; Guthrie, G.B.; Messerly, J.F.; Todd, S.S.; Berg, W.T.; Hossenlopp, I.A.; McCullough, J.P.,
Toluene: Thermodynamic Propoerties, Molecular Vibrations, and Internal Rotation,
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Ziegler and Andrews, 1942
Ziegler, W.T.; Andrews, D.H.,
The heat capacity of benzene-d6,
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Stull, 1937
Stull, D.R.,
A Semi-micro Calorimeter for Measuring Heat Capacities at Low Temp.,
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Kelley, K.K.,
The heat capacity of toluene from 14 deg K to 298 deg K. the entropy and the free energy of formation.,
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Chirico, R.D.; Steele, W.V.,
Reconciliation of Calorimetrically and Spectroscopically Derived Methyl Benzene. The Importance of the Third Virial Coefficient,
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Goodwin, 1989
Goodwin, R.D.,
Toluene thermophysical properties from 178 to 800 K at pressures to 1000 Bar,
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, Report, NIPPR-395, 1988. [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,
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Lenchitz and Velicky, 1970
Lenchitz, Charles; Velicky, Rodolf W.,
Vapor pressure and heat of sublimation of three nitrotoluenes,
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Notes
Go To: Top, Condensed phase thermochemistry data, Phase change data, References
- Symbols used in this document:
Cp,liquid Constant pressure heat capacity of liquid Pc Critical pressure S°liquid Entropy of liquid at standard conditions 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 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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