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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Gas phase thermochemistry data
Go To: Top, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, Gas phase ion energetics data, Ion clustering 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
DRB - Donald R. Burgess, Jr.
GT - Glushko Thermocenter, Russian Academy of Sciences, Moscow
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°gas | -133.6 ± 1.1 | kJ/mol | Ccb | Cox, 1961 | ALS |
ΔfH°gas | -132.3 ± 1.1 | kJ/mol | Ccb | Andon, Biddiscombe, et al., 1960 | ALS |
ΔfH°gas | -117.3 | kJ/mol | N/A | Pushin, 1954 | Value computed using ΔfHliquid° value of -177.0 kj/mol from Pushin, 1954 and ΔvapH° value of 59.7 kj/mol from Cox, 1961.; DRB |
ΔfH°gas | -133.8 | kJ/mol | N/A | Badoche, 1941 | Value computed using ΔfHliquid° value of -193.5 kj/mol from Badoche, 1941 and ΔvapH° value of 59.7 kj/mol from Cox, 1961.; DRB |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
38.69 | 50. | Kudchadker S.A., 1978 | Selected entropies and heat capacities are in close agreement with statistical values calculated by [ Green J.H.S., 1962].; GT |
50.75 | 100. | ||
67.59 | 150. | ||
86.00 | 200. | ||
114.73 | 273.15 | ||
124.68 | 298.15 | ||
125.41 | 300. | ||
162.97 | 400. | ||
194.54 | 500. | ||
219.94 | 600. | ||
240.45 | 700. | ||
257.31 | 800. | ||
271.41 | 900. | ||
283.34 | 1000. | ||
293.51 | 1100. | ||
302.24 | 1200. | ||
309.77 | 1300. | ||
316.28 | 1400. | ||
321.94 | 1500. |
Condensed phase thermochemistry data
Go To: Top, Gas phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, Gas phase ion energetics data, Ion clustering 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
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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)
View plot Requires a JavaScript / HTML 5 canvas capable browser.
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 |
Reaction thermochemistry data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics data, Ion clustering 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
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
C7H7O- + =
By formula: C7H7O- + H+ = C7H8O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1457. ± 5.0 | kJ/mol | CIDC | Angel and Ervin, 2006 | gas phase; B |
ΔrH° | 1462. ± 8.8 | kJ/mol | G+TS | Fujio, McIver, et al., 1981 | gas phase; value altered from reference due to change in acidity scale; B |
ΔrH° | 1467. ± 9.6 | kJ/mol | G+TS | Kebarle and McMahon, 1977 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1434. ± 8.4 | kJ/mol | IMRE | Fujio, McIver, et al., 1981 | gas phase; value altered from reference due to change in acidity scale; B |
ΔrG° | 1438. ± 8.4 | kJ/mol | IMRE | Kebarle and McMahon, 1977 | gas phase; B |
By formula: Br- + C7H8O = (Br- • C7H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 86.2 ± 7.5 | kJ/mol | IMRE | Paul and Kebarle, 1990 | gas phase; ΔGaff at 423 K; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 96. | J/mol*K | N/A | Paul and Kebarle, 1990 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 45.6 ± 4.2 | kJ/mol | IMRE | Paul and Kebarle, 1990 | gas phase; ΔGaff at 423 K; B |
Free energy of reaction
ΔrG° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
45.6 | 423. | PHPMS | Paul and Kebarle, 1990 | gas phase; Entropy change calculated or estimated; M |
By formula: C9H10O2 + H2O = C7H8O + C2H4O2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -18.4 ± 0.59 | kJ/mol | Cm | Sunner, 1957 | liquid phase; Heat of hydrolysis; ALS |
Henry's Law data
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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) = k°H exp(d(ln(kH))/d(1/T) ((1/T) - 1/(298.15 K)))
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)
k°H (mol/(kg*bar)) | d(ln(kH))/d(1/T) (K) | Method | Reference | Comment |
---|---|---|---|---|
1400. | Q | N/A | missing citation give several references for the Henry's law constants but don't assign them to specific species. Value at T = 293. K. | |
620. | 7700. | X | N/A |
Gas phase ion energetics data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, Ion clustering data, References, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data evaluated as indicated in comments:
L - Sharon G. Lias
Data compiled as indicated in comments:
B - John E. Bartmess
MM - Michael M. Meot-Ner (Mautner)
LL - Sharon G. Lias and Joel F. Liebman
LBLHLM - Sharon G. Lias, John E. Bartmess, Joel F. Liebman, John L. Holmes, Rhoda D. Levin, and W. Gary Mallard
LLK - Sharon G. Lias, Rhoda D. Levin, and Sherif A. Kafafi
RDSH - Henry M. Rosenstock, Keith Draxl, Bruce W. Steiner, and John T. Herron
View reactions leading to C7H8O+ (ion structure unspecified)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
IE (evaluated) | 8.29 ± 0.02 | eV | N/A | N/A | L |
Proton affinity at 298K
Proton affinity (kJ/mol) | Reference | Comment |
---|---|---|
841. ± 8. | van Beelen, Koblenz, et al., 2004 | T = 298K; PA derived by authors from GB with protonation entropy equated to Rlnσ(B)/σ(BH+); MM |
Gas basicity at 298K
Gas basicity (review) (kJ/mol) | Reference | Comment |
---|---|---|
809. ± 8. | van Beelen, Koblenz, et al., 2004 | T = 298K; PA derived by authors from GB with protonation entropy equated to Rlnσ(B)/σ(BH+); MM |
Ionization energy determinations
IE (eV) | Method | Reference | Comment |
---|---|---|---|
8.36 ± 0.11 | EI | Selim, Fahmey, et al., 1991 | LL |
8.29 ± 0.02 | S | Oikawa, Abe, et al., 1985 | LBLHLM |
8.23 | EI | Russell, Freiser, et al., 1983 | LBLHLM |
8.52 ± 0.05 | EI | Pignataro, Foffani, et al., 1966 | RDSH |
8.98 | EI | Crable and Kearns, 1962 | RDSH |
8.41 | PE | Palmer, Moyes, et al., 1979 | Vertical value; LLK |
8.52 | PE | Kobayashi and Nagakura, 1974 | Vertical value; LLK |
Appearance energy determinations
Ion | AE (eV) | Other Products | Method | Reference | Comment |
---|---|---|---|---|---|
C6H5+ | 14.60 ± 0.10 | ? | EI | Selim, Fahmey, et al., 1990 | LL |
C6H7+ | 11.37 | ? | EI | Russell, Freiser, et al., 1983 | LBLHLM |
C7H7+ | 11.28 ± 0.05 | OH | EI | Selim, Fahmey, et al., 1990 | LL |
C7H7O+ | 11.17 | H | EI | Russell, Freiser, et al., 1983 | LBLHLM |
C7H7O+ | 12.3 ± 0.1 | H | EI | Tait, Shannon, et al., 1962 | RDSH |
De-protonation reactions
C7H7O- + =
By formula: C7H7O- + H+ = C7H8O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1457. ± 5.0 | kJ/mol | CIDC | Angel and Ervin, 2006 | gas phase; B |
ΔrH° | 1462. ± 8.8 | kJ/mol | G+TS | Fujio, McIver, et al., 1981 | gas phase; value altered from reference due to change in acidity scale; B |
ΔrH° | 1467. ± 9.6 | kJ/mol | G+TS | Kebarle and McMahon, 1977 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1434. ± 8.4 | kJ/mol | IMRE | Fujio, McIver, et al., 1981 | gas phase; value altered from reference due to change in acidity scale; B |
ΔrG° | 1438. ± 8.4 | kJ/mol | IMRE | Kebarle and McMahon, 1977 | gas phase; B |
Ion clustering data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, Gas phase ion energetics 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
Note: Please consider using the reaction search for this species. This page allows searching of all reactions involving this species. Searches may be limited to ion clustering reactions. A general reaction search form is also available.
Clustering reactions
By formula: Br- + C7H8O = (Br- • C7H8O)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 86.2 ± 7.5 | kJ/mol | IMRE | Paul and Kebarle, 1990 | gas phase; ΔGaff at 423 K; B,M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 96. | J/mol*K | N/A | Paul and Kebarle, 1990 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 45.6 ± 4.2 | kJ/mol | IMRE | Paul and Kebarle, 1990 | gas phase; ΔGaff at 423 K; B |
Free energy of reaction
ΔrG° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
45.6 | 423. | PHPMS | Paul and Kebarle, 1990 | gas phase; Entropy change calculated or estimated; M |
References
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, Gas phase ion energetics data, Ion clustering 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]
Kudchadker S.A., 1978
Kudchadker S.A.,
Ideal gas thermodynamic properties of phenol and cresols,
J. Phys. Chem. Ref. Data, 1978, 7, 417-423. [all data]
Green J.H.S., 1962
Green J.H.S.,
Normal frequencies, thermodynamic properties and equilibrium of the cresols,
Chem. Ind. (London), 1962, 1575-1576. [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.,
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Goldblum, Martin, et al., 1947
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Notes
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, Gas phase ion energetics data, Ion clustering data, References
- Symbols used in this document:
AE Appearance energy Cp,gas Constant pressure heat capacity of gas Cp,liquid Constant pressure heat capacity of liquid IE (evaluated) Recommended ionization energy Pc Critical pressure S°liquid Entropy of liquid at standard conditions T Temperature Tboil Boiling point Tc Critical temperature Tfus Fusion (melting) point Ttriple Triple point temperature d(ln(kH))/d(1/T) Temperature dependence parameter for Henry's Law constant k°H Henry's Law constant at 298.15K ΔcH°liquid Enthalpy of combustion of liquid at standard conditions ΔfH°gas Enthalpy of formation of gas at standard conditions ΔfH°liquid Enthalpy of formation of liquid at standard conditions ΔfusH Enthalpy of fusion ΔfusS Entropy of fusion ΔrG° Free energy of reaction at standard conditions ΔrH° Enthalpy of reaction at standard conditions ΔrS° Entropy of reaction at standard conditions 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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