Phenol, 3-methyl-
- Formula: C7H8O
- Molecular weight: 108.1378
- IUPAC Standard InChIKey: RLSSMJSEOOYNOY-UHFFFAOYSA-N
- CAS Registry Number: 108-39-4
- 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. - Other names: m-Cresol; m-Cresole; m-Cresylic acid; m-Hydroxytoluene; m-Kresol; m-Methylphenol; m-Oxytoluene; m-Toluol; 1-Hydroxy-3-methylbenzene; 3-Cresol; 3-Hydroxytoluene; 3-Methylphenol; meta-Cresol; Cresol, meta; Rcra waste number U052; Cresol,m-; NSC 8768
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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 |
---|---|---|---|---|---|
ΔfH°liquid | -193.3 | kJ/mol | Ccb | Cox, 1961 | ALS |
ΔfH°liquid | -194.1 ± 1.1 | kJ/mol | Ccb | Andon, Biddiscombe, et al., 1960 | ALS |
ΔfH°liquid | -177. | kJ/mol | Ccb | Pushin, 1954 | Author's hf298_condensed=-44.4 kcal/mol; ALS |
ΔfH°liquid | -193.5 | kJ/mol | Ccb | Badoche, 1941 | Author's hf298_condensed=-48.97 kcal/mol; ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -3704.7 ± 0.3 | kJ/mol | Ccb | Cox, 1961 | Corresponding ΔfHºliquid = -193.2 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -3703.9 ± 0.59 | kJ/mol | Ccb | Andon, Biddiscombe, et al., 1960 | Corresponding ΔfHºliquid = -194.0 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -3721. | kJ/mol | Ccb | Pushin, 1954 | Author's hf298_condensed=-44.4 kcal/mol; Corresponding ΔfHºliquid = -177. kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -3704.4 | kJ/mol | Ccb | Badoche, 1941 | Author's hf298_condensed=-48.97 kcal/mol; Corresponding ΔfHºliquid = -193.5 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -3694. | kJ/mol | Ccb | Barker, 1925 | Author was aware that data differs from previously reported values; Corresponding ΔfHºliquid = -203. kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
Quantity | Value | Units | Method | Reference | Comment |
S°liquid | 212.59 | J/mol*K | N/A | Andon, Counsell, et al., 1967 | DH |
Constant pressure heat capacity of liquid
Cp,liquid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
224.93 | 298.15 | Andon, Counsell, et al., 1967 | T = 10 to 400 K.; DH |
220.9 | 93. | Rastorguev and Ganiev, 1967 | T = 293 to 373 K.; DH |
218.8 | 298. | Tschamler and Krischai, 1951 | DH |
216.7 | 283. | Bramley, 1916 | Mean value, 0 to 20 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
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 |
---|---|---|---|---|---|
Tboil | 475.2 ± 0.9 | K | AVG | N/A | Average of 18 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 284. ± 4. | K | AVG | N/A | Average of 16 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 285.40 | K | N/A | Andon, Counsell, et al., 1967, 2 | Uncertainty assigned by TRC = 0.02 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 705.8 | K | N/A | Delaunois, 1968 | Uncertainty assigned by TRC = 0.4 K; TRC |
Tc | 705.75 | K | N/A | Ambrose, 1963 | Uncertainty assigned by TRC = 0.45 K; TRC |
Tc | 705.15 | K | N/A | Glaser and Ruland, 1957 | Uncertainty assigned by TRC = 2. K; TRC |
Tc | 705.0 | K | N/A | Guye and Mallet, 1902 | Uncertainty assigned by TRC = 2.5 K; TRC |
Tc | 705.15 | K | N/A | Guye and Mallet, 1902, 2 | Uncertainty assigned by TRC = 2. K; accomipanied by some decomposition; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 43.60 | bar | N/A | Delaunois, 1968 | Uncertainty assigned by TRC = 5.884 bar; TRC |
Pc | 45.5963 | bar | N/A | Glaser and Ruland, 1957 | Uncertainty assigned by TRC = 3.0398 bar; TRC |
Pc | 45.60 | bar | N/A | Guye and Mallet, 1902 | Uncertainty assigned by TRC = 0.9119 bar; TRC |
Pc | 45.5456 | bar | N/A | Guye and Mallet, 1902, 2 | Uncertainty assigned by TRC = 1.5199 bar; TRC |
Pc | 45.6469 | bar | N/A | Guye and Mallet, 1902, 2 | Uncertainty assigned by TRC = 1.5199 bar; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 60. ± 10. | kJ/mol | AVG | N/A | Average of 8 values; Individual data points |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
63.1 | 300. | A | Stephenson and Malanowski, 1987 | Based on data from 285. to 416. K.; AC |
52.7 | 425. | A | Stephenson and Malanowski, 1987 | Based on data from 410. to 477. K.; AC |
47.6 | 486. | A | Stephenson and Malanowski, 1987 | Based on data from 471. to 531. K.; AC |
43.8 | 538. | A | Stephenson and Malanowski, 1987 | Based on data from 523. to 633. K.; AC |
55.0 | 398. | GS,EB | Stephenson and Malanowski, 1987 | Based on data from 383. to 473. K. See also Andon, Biddiscombe, et al., 1960, 2.; AC |
60.6 | 409. | GS | Nasir, Hwang, et al., 1980 | Based on data from 388. to 429. K. See also Kkykj and Repas, 1973.; AC |
58.8 | 374. | N/A | von Terres, Gebert, et al., 1955 | Based on data from 359. to 473. K. See also Boublik, Fried, et al., 1984.; AC |
50.7 | 448. | N/A | Goldblum, Martin, et al., 1947 | Based on data from 422. to 474. K.; AC |
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 |
---|---|---|---|---|---|
422.7 to 474.3 | 4.60157 | 1833.137 | -76.414 | Goldblum, Martin, et al., 1947 | Coefficents calculated by NIST from author's data. |
Enthalpy of sublimation
ΔsubH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
56.1 | 279. | A | Stephenson and Malanowski, 1987 | Based on data from 273. to 285. K.; AC |
61.7 ± 1.0 | 284. to 313. | GS | Andon, Biddiscombe, et al., 1960, 2 | AC |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
9.100 | 280.75 | N/A | Meva'a and Lichanot, 1990 | DH |
9.413 | 285.0 | N/A | Poeti, Fanelli, et al., 1982 | DH |
10.707 | 285.40 | N/A | Andon, Counsell, et al., 1967 | DH |
8.9 | 282.3 | DSC | Richard, Bernardes, et al., 2007 | AC |
10.67 | 285.3 | DSC | Jamróz, Palczewska-Tulinska, et al., 1998 | AC |
10.71 | 285.4 | N/A | Domalski and Hearing, 1996 | AC |
9.1 | 280.8 | N/A | Meva'a and Lichanot, 1990 | AC |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
32. | 280.75 | Meva'a and Lichanot, 1990 | DH |
33.03 | 285.0 | Poeti, Fanelli, et al., 1982 | DH |
27.53 | 285.40 | Andon, Counsell, et al., 1967 | 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.
Cox, 1961
Cox, J.D.,
The heats of combustion of phenol and the three cresols,
Pure Appl. Chem., 1961, 2, 125-128. [all data]
Andon, Biddiscombe, et al., 1960
Andon, R.J.L.; Biddiscombe, D.P.; Cox, J.D.; Handley, R.; Harrop, D.; Herington, E.F.G.; Martin, J.F.,
Thermodynamic properties of organic oxygen compounds. Part I. Preparation and physical properties of pure phenol, cresols, and xylenols,
J. Chem. Soc., 1960, 5246-5254. [all data]
Pushin, 1954
Pushin, N.A.,
Heats of combustion and heats of formation of isomeric organic compounds,
Bull. Soc. Chim. Belgrade, 1954, 19, 531-547. [all data]
Badoche, 1941
Badoche, M.,
No 19. - Chaleurs de combustion du phenol, du-m-cresol et del leurs ethers; par M. Marius BADOCHE.,
Bull. Soc. Chim. Fr., 1941, 8, 212-220. [all data]
Barker, 1925
Barker, M.F.,
Calorific value and constitution,
J. Phys. Chem., 1925, 29, 1345-1363. [all data]
Andon, Counsell, et al., 1967
Andon, R.J.L.; Counsell, J.F.; Lees, E.B.; Martin, J.F.; Mash, C.J.,
Thermodynamic properties of organic oxygen compounds. Part 17. Low-temperature heat capacity and entropy of the cresols,
Trans. Faraday Soc., 1967, 63, 1115-1121. [all data]
Rastorguev and Ganiev, 1967
Rastorguev, Yu.L.; Ganiev, Yu.A.,
Study of the heat capacity of selected solvents,
Izv. Vyssh. Uchebn. Zaved. Neft Gaz. 10, 1967, No.1, 79-82. [all data]
Tschamler and Krischai, 1951
Tschamler, H.; Krischai, H.,
Chinolin-m-Kresol, ein stark negatives System,
Monatsh. Chem., 1951, 82, 259-270. [all data]
Bramley, 1916
Bramley, A.,
The study of binary mixtures. Part IV. Heats of reaction and specific heats,
J. Chem. Soc. (London), 1916, 109, 496-515. [all data]
Andon, Counsell, et al., 1967, 2
Andon, R.J.L.; Counsell, J.F.; Lees, E.B.; Martin, J.F.; Mash, C.J.,
Thermodynamic Properties of Organic Oxygen Compounds Part 17. Low- temperature Heat Capacity and Entropy of the Cresols,
Trans. Faraday Soc., 1967, 63, 1115. [all data]
Delaunois, 1968
Delaunois, C.,
Effect of the Filling Rate of a Reactor on the Vapor Tension and the Temperature at the Beginning of Cracking of Phenols at High Pressures,
Ann. Mines Belg., 1968, No. 1, 9-16. [all data]
Ambrose, 1963
Ambrose, D.,
Critical Temperatures of Some Phenols and Other Organic Compounds,
Trans. Faraday Soc., 1963, 59, 1988. [all data]
Glaser and Ruland, 1957
Glaser, F.; Ruland, H.,
Untersuchungsen über dampfdruckkurven und kritische daten einiger technisch wichtiger organischer substanzen,
Chem. Ing. Techn., 1957, 29, 772. [all data]
Guye and Mallet, 1902
Guye, P.A.; Mallet, E.,
Critical Constant and Molecular Complexity of Several Organic Compds.,
C. R. Hebd. Seances Acad. Sci., 1902, 133, 168. [all data]
Guye and Mallet, 1902, 2
Guye, P.A.; Mallet, E.,
Measurement of Critical Constants,
Arch. Sci. Phys. Nat., 1902, 13, 274-296. [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]
Andon, Biddiscombe, et al., 1960, 2
Andon, R.J.L.; Biddiscombe, D.P.; Cox, J.D.; Handley, R.; Harrop, D.; Herington, E.F.G.; Martin, J.F.,
1009. Thermodynamic properties of organic oxygen compounds. Part I. Preparation and physical properties of pure phenol, cresols, and xylenols,
J. Chem. Soc., 1960, 5246, https://doi.org/10.1039/jr9600005246
. [all data]
Nasir, Hwang, et al., 1980
Nasir, P.; Hwang, S.C.; Kobayashi, R.,
Development of an apparatus to measurement vapor pressures at high temperatures and its application to three higher-boiling compounds,
J. Chem. Eng. Data, 1980, 25, 4, 298-301, https://doi.org/10.1021/je60087a009
. [all data]
Kkykj and Repas, 1973
Kkykj, J.; Repas, M.,
Petrochemia, 1973, 13, 179. [all data]
von Terres, Gebert, et al., 1955
von Terres, E.; Gebert, F.; Hulsemann, H.; Petereit, H.; Toepsch, H.; Ruppert, W.,
Brennst.-Chem., 1955, 36, 272. [all data]
Boublik, Fried, et al., 1984
Boublik, T.; Fried, V.; Hala, E.,
The Vapour Pressures of Pure Substances: Selected Values of the Temperature Dependence of the Vapour Pressures of Some Pure Substances in the Normal and Low Pressure Region, 2nd ed., Elsevier, New York, 1984, 972. [all data]
Goldblum, Martin, et al., 1947
Goldblum, K.B.; Martin, R.W.; Young, R.B.,
Vapor Pressure Data for Phenols,
Ind. Eng. Chem., 1947, 39, 11, 1474-1476, https://doi.org/10.1021/ie50455a017
. [all data]
Meva'a and Lichanot, 1990
Meva'a, L.M.; Lichanot, A.,
Proprietes thermodynamiques en phase condensee des ortho, meta et para fluorotoluene, cresol et toluidine,
Thermochim. Acta, 1990, 158, 335-345. [all data]
Poeti, Fanelli, et al., 1982
Poeti, G.; Fanelli, E.; Braghetti, M.,
A differential scanning calorimetric study of some phenol derivatives,
J. Therm. Anal., 1982, 24(2), 273-279. [all data]
Richard, Bernardes, et al., 2007
Richard, Laurence S.; Bernardes, Carlos E.S.; Diogo, Hermínio P.; Leal, João P.; Minas da Piedade, Manuel E.,
Energetics of Cresols and of Methylphenoxyl Radicals,
J. Phys. Chem. A, 2007, 111, 35, 8741-8748, https://doi.org/10.1021/jp073515m
. [all data]
Jamróz, Palczewska-Tulinska, et al., 1998
Jamróz, Malgorzata E.; Palczewska-Tulinska, Marcela; Wyrzykowska-Stankiewicz, Danuta; Szafranski, Andrzej M.; Polaczek, Jerzy; Dobrowolski, Jan Cz.; Jamróz, Michal H.; Mazurek, Aleksander P.,
The urea--phenol(s) systems,
Fluid Phase Equilibria, 1998, 152, 2, 307-326, https://doi.org/10.1016/S0378-3812(98)90206-0
. [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]
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 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 ΔvapH Enthalpy of vaporization ΔvapH° Enthalpy of vaporization at standard conditions - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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