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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Phase change data
Go To: Top, 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 | 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 | 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, 2 | DH |
6.619 | 177.95 | Kelley, 1929, 2 | 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, 2 | DH |
37.20 | 177.95 | Kelley, 1929, 2 | DH |
36.79 | 178.0 | Ziegler and Andrews, 1942, 2 | DH |
References
Go To: Top, Phase change data, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
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 Propoerties, Molecular Vibrations, and Internal Rotation,
J. Phys. Chem., 1962, 66, 911-4. [all data]
Ziegler and Andrews, 1942
Ziegler, W.T.; Andrews, D.H.,
The heat capacity of benzene-d6,
J. Am. Chem. Soc., 1942, 64, 2482. [all data]
Stull, 1937
Stull, D.R.,
A Semi-micro Calorimeter for Measuring Heat Capacities at Low Temp.,
J. Am. Chem. Soc., 1937, 59, 2726. [all data]
Kelley, 1929
Kelley, K.K.,
The heat capacity of toluene from 14 deg K to 298 deg K. the entropy and the free energy of formation.,
J. Am. Chem. Soc., 1929, 51, 2738. [all data]
Tsonopoulos and Ambrose, 1995
Tsonopoulos, C.; Ambrose, D.,
Vapor-Liquid Critical Properties of Elements and Compounds. 3. Aromatic Hydrocarbons,
J. Chem. Eng. Data, 1995, 40, 547-558. [all data]
Chirico and Steele, 1994
Chirico, R.D.; Steele, W.V.,
Reconciliation of Calorimetrically and Spectroscopically Derived Methyl Benzene. The Importance of the Third Virial Coefficient,
Ind. Eng. Chem. Res., 1994, 33, 157-67. [all data]
Goodwin, 1989
Goodwin, R.D.,
Toluene thermophysical properties from 178 to 800 K at pressures to 1000 Bar,
J. Phys. Chem. Ref. Data, 1989, 18, 1565-636. [all data]
Steele, Chirico, et al., 1988
Steele, W.V.; Chirico, R.D.; Knipmeyer, S.E.; Smith, N.K.,
, 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,
Bull. Soc. Chim. Belg., 1957, 66, 375-81. [all data]
Lenchitz and Velicky, 1970
Lenchitz, Charles; Velicky, Rodolf W.,
Vapor pressure and heat of sublimation of three nitrotoluenes,
J. Chem. Eng. Data, 1970, 15, 3, 401-403, https://doi.org/10.1021/je60046a022
. [all data]
Weast and Grasselli, 1989
CRC Handbook of Data on Organic Compounds, 2nd Editon, Weast,R.C and Grasselli, J.G., ed(s)., CRC Press, Inc., Boca Raton, FL, 1989, 1. [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]
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]
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]
Forziati, Norris, et al., 1949
Forziati, Alphonse F.; Norris, William R.; Rossini, Frederick D.,
Vapor pressures and boiling points of sixty API-NBS hydrocarbons,
J. RES. NATL. BUR. STAN., 1949, 43, 6, 555-17, https://doi.org/10.6028/jres.043.050
. [all data]
Natarajan and Viswanath, 1985
Natarajan, Govindarajan; Viswanath, Dabir S.,
Enthalpy of vaporization and vapor pressure of benzene, toluene, p-xylene, and tetralin between 1 and 16 bar,
J. Chem. Eng. Data, 1985, 30, 2, 137-140, https://doi.org/10.1021/je00040a001
. [all data]
Eubank, Cediel, et al., 1984
Eubank, P.T.; Cediel, L.E.; Holste, J.C.; Hall, K.R.,
Enthalpies for toluene and methylcyclohexane in the fluid state,
J. Chem. Eng. Data, 1984, 29, 389-393. [all data]
Rivenq, 1975
Rivenq, F.,
Bull. Soc. Chim. Fr., 1975, 1, 2433. [all data]
Gaw and Swinton, 1968
Gaw, W.J.; Swinton, F.L.,
Thermodynamic properties of binary systems containing hexafluorobenzene. Part 4.?Excess Gibbs free energies of the three systems hexafluorobenzene + benzene, touene, and p-xylene,
Trans. Faraday Soc., 1968, 64, 2023, https://doi.org/10.1039/tf9686402023
. [all data]
Van Ness, Soczek, et al., 1967
Van Ness, Hendrick C.; Soczek, C.A.; Peloquin, G.L.; Machado, R.L.,
Thermodynamic excess properties of three alcohol-hydrocarbon systems,
J. Chem. Eng. Data, 1967, 12, 2, 217-224, https://doi.org/10.1021/je60033a017
. [all data]
Scott, Gutherie, et al., 1962
Scott, D.W.; Gutherie, 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. [all data]
Milazzo, 1956
Milazzo, G.,
Ann. Chim. (Rome), 1956, 46, 1105. [all data]
Thomson, 1946
Thomson, George Wm.,
The Antoine Equation for Vapor-pressure Data.,
Chem. Rev., 1946, 38, 1, 1-39, https://doi.org/10.1021/cr60119a001
. [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]
Pitzer and Scott, 1943
Pitzer, K.S.; Scott, D.W.,
The thermodynamics and molecular structure of benzene and its methyl derivatives,
J. Am. Chem. Soc., 1943, 65, 803-829. [all data]
Besley and Bottomley, 1974
Besley, L.M.; Bottomley, G.A.,
Vapour Pressure of Toluene from 273.15 to 298.15 K,
J. Chem. Thermodyn., 1974, 6, 6, 577-580, https://doi.org/10.1016/0021-9614(74)90045-7
. [all data]
Gaw and Swinton, 1968, 2
Gaw, W.J.; Swinton, F.L.,
Thermodynamic Properties of Binary Systems Containing Hexafluorobenzene. Part 3. Excess Gibbs Free Energy of the System Hexafluorobenzene + Cyclohexane,
Trans. Faraday Soc., 1968, 64, 637-647, https://doi.org/10.1039/tf9686400637
. [all data]
Ambrose, Broderick, et al., 1967
Ambrose, D.; Broderick, B.E.; Townsend, R.,
The Vapour Pressures Above the Normal Boiling Point and the Critical Pressures of Some Aromatic Hydrocarbons,
J. Chem. Soc. A:, 1967, 633-641, https://doi.org/10.1039/j19670000633
. [all data]
Williamham, Taylor, et al., 1945
Williamham, 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. Stand. (U.S.), 1945, 35, 3, 219-244, https://doi.org/10.6028/jres.035.009
. [all data]
Scott, Guthrie, et al., 1962, 2
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, 2
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]
Ziegler and Andrews, 1942, 2
Ziegler, W.T.; Andrews, D.H.,
The heat capacity of benzene-d6,
J. Am. Chem. Soc., 1942, 64, 2482-2485. [all data]
Domalski and Hearing, 1996
Domalski, Eugene S.; Hearing, Elizabeth D.,
Heat Capacities and Entropies of Organic Compounds in the Condensed Phase. Volume III,
J. Phys. Chem. Ref. Data, 1996, 25, 1, 1, https://doi.org/10.1063/1.555985
. [all data]
Southard and Andrews, 1930
Southard, John C.; Andrews, Donald H.,
The heat capacities of organic compounds at low temperatures. iii. an adiabatic calorimeter for heat capacities at low temperatures,
Journal of the Franklin Institute, 1930, 209, 3, 349-360, https://doi.org/10.1016/S0016-0032(30)90040-3
. [all data]
Notes
Go To: Top, Phase change data, References
- Symbols used in this document:
Pc Critical pressure Tboil Boiling point Tc Critical temperature Tfus Fusion (melting) point Ttriple Triple point temperature Vc Critical volume 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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