Methyl Alcohol
- Formula: CH4O
- Molecular weight: 32.0419
- IUPAC Standard InChIKey: OKKJLVBELUTLKV-UHFFFAOYSA-N
- CAS Registry Number: 67-56-1
- 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: Methanol; Carbinol; Methyl hydroxide; Methylol; Monohydroxymethane; Wood alcohol; CH3OH; Colonial spirit; Columbian spirit; Hydroxymethane; Wood naphtha; Alcool methylique; Alcool metilico; Columbian spirits; Metanolo; Methylalkohol; Metylowy alkohol; Pyroxylic spirit; Wood spirit; Rcra waste number U154; UN 1230; Pyro alcohol; Spirit of wood; Bieleski's solution; NSC 85232
- Permanent link for this species. Use this link for bookmarking this species for future reference.
- Information on this page:
- Other data available:
- Condensed phase thermochemistry data
- Reaction thermochemistry data: reactions 1 to 50, reactions 51 to 100, reactions 101 to 150, reactions 151 to 200, reactions 201 to 250, reactions 251 to 300
- Ion clustering data
- IR Spectrum
- Mass spectrum (electron ionization)
- Vibrational and/or electronic energy levels
- Gas Chromatography
- Fluid Properties
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Gas phase thermochemistry data
Go To: Top, Phase change 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:
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 | -205. ± 10. | kJ/mol | AVG | N/A | Average of 9 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°gas | -763.68 ± 0.20 | kJ/mol | Cm | Rossini, 1932 | Flame Calorimetry; Corresponding ΔfHºgas = -201.49 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
34.00 | 50. | Thermodynamics Research Center, 1997 | p=1 bar. Recommended entropies and heat capacities are in good agreement with other statistically calculated values [ Ivash E.V., 1955, Zhuravlev E.Z., 1959, Chen S.S., 1977, Chao J., 1986, Gurvich, Veyts, et al., 1989]. Please also see Chao J., 1986, 2.; GT |
36.95 | 100. | ||
38.64 | 150. | ||
39.71 | 200. | ||
42.59 | 273.15 | ||
44.06 ± 0.03 | 298.15 | ||
44.17 | 300. | ||
51.63 | 400. | ||
59.70 | 500. | ||
67.19 | 600. | ||
73.86 | 700. | ||
79.76 | 800. | ||
84.95 | 900. | ||
89.54 | 1000. | ||
93.57 | 1100. | ||
97.12 | 1200. | ||
100.24 | 1300. | ||
102.98 | 1400. | ||
105.40 | 1500. | ||
110.2 | 1750. | ||
113.8 | 2000. | ||
116.5 | 2250. | ||
118.6 | 2500. | ||
120. | 2750. | ||
121. | 3000. |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
42.4 ± 1.3 | 279. | Stromsoe E., 1970 | Heat capacity at 279 K was obtained by thermal conductivity [ Halford J.O., 1957]. Vapor heat capacities from calorimetric measurements [ De Vries T., 1941] were converted to the ideal gas heat capacities by corrections for the gas imperfection effects [ Chen S.S., 1977, Chao J., 1986, 2]. Ideal gas heat capacities are given by [ Stromsoe E., 1970] as a linear function Cp=f1*(a+bT). This expression approximates the experimental values with the average deviation of 1.17 J/mol*K. The accuracy of the experimental heat capacities [ Stromsoe E., 1970] is estimated as less than 0.3%. Please also see De Vries T., 1941, Weltner W., 1951, Halford J.O., 1957.; GT |
48.0 ± 1.3 | 345.6 | ||
46.8 ± 1.2 | 347.35 | ||
46.1 ± 1.3 | 349.65 | ||
47.6 ± 1.2 | 356.55 | ||
46.7 ± 1.3 | 358.15 | ||
48.2 ± 1.3 | 358.85 | ||
48.8 ± 1.3 | 359.85 | ||
50.3 ± 1.3 | 368.15 | ||
49.0 ± 1.2 | 373.35 | ||
51.3 ± 1.3 | 382.15 | ||
51.1 ± 1.2 | 398.95 | ||
52.3 ± 1.3 | 401.15 | ||
51.3 ± 1.2 | 401.35 | ||
52.01 ± 0.42 | 403.2 | ||
53.2 ± 1.3 | 420.15 | ||
53.9 ± 1.2 | 431.45 | ||
54.8 ± 1.2 | 442.15 | ||
55.9 ± 1.3 | 442.65 | ||
56.0 ± 1.2 | 457.35 | ||
57.20 ± 0.42 | 464.0 | ||
57.8 ± 1.2 | 477.75 | ||
58.4 ± 1.2 | 485.05 | ||
59.5 ± 1.2 | 498.95 | ||
60.4 ± 1.3 | 521.2 | ||
61.4 ± 1.2 | 521.35 | ||
64.3 ± 1.2 | 555.95 | ||
66.4 ± 1.2 | 581.35 | ||
66.8 ± 1.2 | 585.35 |
Phase change data
Go To: Top, Gas phase 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:
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, Chris Muzny director
DH - Eugene S. Domalski and Elizabeth D. Hearing
AC - William E. Acree, Jr., James S. Chickos
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
DRB - Donald R. Burgess, Jr.
CAL - James S. Chickos, William E. Acree, Jr., Joel F. Liebman, Students of Chem 202 (Introduction to the Literature of Chemistry), University of Missouri -- St. Louis
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 337.8 ± 0.3 | K | AVG | N/A | Average of 154 out of 171 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 176. ± 1. | K | AVG | N/A | Average of 13 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 175.5 ± 0.5 | K | AVG | N/A | Average of 8 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 513. ± 1. | K | AVG | N/A | Average of 27 out of 31 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 81. ± 1. | bar | AVG | N/A | Average of 17 out of 20 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Vc | 0.117 | l/mol | N/A | Gude and Teja, 1995 | |
Vc | 0.113024 | l/mol | N/A | Craven and de Reuck, 1986 | TRC |
Vc | 0.118 | l/mol | N/A | Francesconi, Lentz, et al., 1981 | Uncertainty assigned by TRC = 0.004 l/mol; TRC |
Vc | 0.11663 | l/mol | N/A | Zubarev and Bagdonas, 1969 | Uncertainty assigned by TRC = 0.0035 l/mol; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 8.51 ± 0.07 | mol/l | AVG | N/A | Average of 7 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 37.6 ± 0.5 | kJ/mol | AVG | N/A | Average of 11 out of 12 values; Individual data points |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
35.21 | 337.7 | N/A | Majer and Svoboda, 1985 | |
39.2 | 258. | A | Stephenson and Malanowski, 1987 | Based on data from 175. to 273. K.; AC |
36.9 | 353. | A | Stephenson and Malanowski, 1987 | Based on data from 338. to 487. K.; AC |
43.7 | 213. | A | Stephenson and Malanowski, 1987 | Based on data from 188. to 228. K.; AC |
38.9 | 275. | A | Stephenson and Malanowski, 1987 | Based on data from 224. to 290. K.; AC |
38.3 | 300. | A | Stephenson and Malanowski, 1987 | Based on data from 285. to 345. K.; AC |
37.0 | 350. | A | Stephenson and Malanowski, 1987 | Based on data from 335. to 376. K.; AC |
36.1 | 388. | A | Stephenson and Malanowski, 1987 | Based on data from 373. to 458. K.; AC |
35.1 | 468. | A | Stephenson and Malanowski, 1987 | Based on data from 453. to 513. K.; AC |
32.7 | 373. | C | Yerlett and Wormald, 1986 | AC |
28.1 | 423. | C | Yerlett and Wormald, 1986 | AC |
20.6 | 473. | C | Yerlett and Wormald, 1986 | AC |
7.4 | 510. | C | Yerlett and Wormald, 1986 | AC |
37.5 | 331. | EB | Cervenkova and Boublik, 1984 | Based on data from 316. to 336. K.; AC |
38.3 | 303. | N/A | Gibbard and Creek, 1974 | Based on data from 288. to 337. K. See also Boublik, Fried, et al., 1984.; AC |
35.2 ± 0.1 | 338. | C | Counsell and Lee, 1973 | AC |
35.6 ± 0.1 | 331. | C | Counsell and Lee, 1973 | AC |
36.2 ± 0.1 | 321. | C | Counsell and Lee, 1973 | AC |
37.0 ± 0.1 | 306. | C | Counsell and Lee, 1973 | AC |
36.7 ± 0.1 | 313. | C | Svoboda, Veselý, et al., 1973 | AC |
36.2 ± 0.1 | 323. | C | Svoboda, Veselý, et al., 1973 | AC |
35.6 ± 0.1 | 333. | C | Svoboda, Veselý, et al., 1973 | AC |
35.3 ± 0.1 | 338. | C | Svoboda, Veselý, et al., 1973 | AC |
34.7 ± 0.1 | 343. | C | Svoboda, Veselý, et al., 1973 | AC |
37.0 | 352. | N/A | Wilhoit and Zwolinski, 1973 | Based on data from 337. to 383. K.; AC |
38.7 | 290. | EB | Boublík and Aim, 1972 | Based on data from 275. to 336. K. See also Stephenson and Malanowski, 1987.; AC |
38.3 | 303. | EB | Ambrose and Sprake, 1970 | Based on data from 288. to 357. K.; AC |
36.3 | 368. | N/A | Hirata, Suda, et al., 1967 | Based on data from 353. to 483. K.; AC |
38.4 | 293. | N/A | Klyueva, Mischenko, et al., 1960 | Based on data from 278. to 323. K.; AC |
Enthalpy of vaporization
ΔvapH = A exp(-αTr)
(1 − Tr)β
ΔvapH =
Enthalpy of vaporization (at saturation pressure)
(kJ/mol)
Tr = reduced temperature (T / Tc)
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Temperature (K) | 298. to 477. |
---|---|
A (kJ/mol) | 45.3 |
α | -0.31 |
β | 0.4241 |
Tc (K) | 512.6 |
Reference | 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 |
---|---|---|---|---|---|
353.5 to 512.63 | 5.15853 | 1569.613 | -34.846 | Ambrose, Sprake, et al., 1975 | Coefficents calculated by NIST from author's data. |
288.1 to 356.83 | 5.20409 | 1581.341 | -33.50 | Ambrose and Sprake, 1970 | Coefficents calculated by NIST from author's data. |
353. to 483. | 5.31301 | 1676.569 | -21.728 | Hirata and Suda, 1967 | Coefficents calculated by NIST from author's data. |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
3.18 | 175.3 | Domalski and Hearing, 1996 | AC |
2.196 | 176. | Maass and Walbauer, 1925 | DH |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
12.5 | 176. | Maass and Walbauer, 1925 | DH |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
3.7 | 161.1 | Domalski and Hearing, 1996 | CAL |
18.1 | 175.3 | ||
4.0 | 157.3 | ||
18.3 | 175.6 |
Enthalpy of phase transition
ΔHtrs (kJ/mol) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
0.6360 | 157.34 | crystaline, II | crystaline, I | Carlson and Westrum, 1971 | DH |
3.2154 | 175.59 | crystaline, I | liquid | Carlson and Westrum, 1971 | DH |
1.540 | 103. | crystaline | glass | Sugisaki, Suga, et al., 1968 | Glass transition.; DH |
0.711 | 157.8 | crystaline, II | crystaline, I | Staveley and Gupta, 1949 | DH |
3.159 | 175.4 | crystaline, I | liquid | Staveley and Gupta, 1949 | DH |
0.6456 | 157.4 | crystaline, II | crystaline, I | Kelley, 1929 | DH |
3.167 | 175.2 | crystaline, I | liquid | Kelley, 1929 | DH |
0.590 | 161.1 | crystaline, II | crystaline, I | Parks, 1925 | DH |
3.176 | 175.3 | crystaline, I | liquid | Parks, 1925 | DH |
Entropy of phase transition
ΔStrs (J/mol*K) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
4.04 | 157.34 | crystaline, II | crystaline, I | Carlson and Westrum, 1971 | DH |
18.31 | 175.59 | crystaline, I | liquid | Carlson and Westrum, 1971 | DH |
14.95 | 103. | crystaline | glass | Sugisaki, Suga, et al., 1968 | Glass; DH |
4.51 | 157.8 | crystaline, II | crystaline, I | Staveley and Gupta, 1949 | DH |
18.01 | 175.4 | crystaline, I | liquid | Staveley and Gupta, 1949 | DH |
4.10 | 157.4 | crystaline, II | crystaline, I | Kelley, 1929 | DH |
18.08 | 175.2 | crystaline, I | liquid | Kelley, 1929 | DH |
3.66 | 161.1 | crystaline, II | crystaline, I | Parks, 1925 | DH |
18.12 | 175.3 | crystaline, I | liquid | Parks, 1925 | DH |
Henry's Law data
Go To: Top, Gas phase thermochemistry data, Phase change 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 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 |
---|---|---|---|---|
140. | Q | N/A | missing citation give several references for the Henry's law constants but don't assign them to specific species. | |
220. | X | N/A | ||
220. | 5200. | M | N/A | |
220. | X | N/A | Value given here as quoted by missing citation. | |
160. | 5600. | X | N/A | |
230. | M | N/A | ||
210. | M,X | Timmermans, 1960 | Value given here as quoted by missing citation. | |
230. | M | Butler, Ramchandani, et al., 1935 | This paper supersedes earlier work with more concentrated solutions Butler, Thomson, et al., 1933. |
Gas phase ion energetics data
Go To: Top, Gas phase thermochemistry data, Phase change 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 evaluated as indicated in comments:
HL - Edward P. Hunter and Sharon G. Lias
L - Sharon G. Lias
Data compiled as indicated in comments:
B - John E. Bartmess
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 CH4O+ (ion structure unspecified)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
IE (evaluated) | 10.84 ± 0.01 | eV | N/A | N/A | L |
Quantity | Value | Units | Method | Reference | Comment |
Proton affinity (review) | 754.3 | kJ/mol | N/A | Hunter and Lias, 1998 | HL |
Quantity | Value | Units | Method | Reference | Comment |
Gas basicity | 724.5 | kJ/mol | N/A | Hunter and Lias, 1998 | HL |
Ionization energy determinations
Appearance energy determinations
De-protonation reactions
CH3O- + =
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1597. ± 8. | kJ/mol | AVG | N/A | Average of 6 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1573.3 ± 2.6 | kJ/mol | H-TS | Nee, Osterwalder, et al., 2006 | gas phase; B |
ΔrG° | 1573.4 ± 2.3 | kJ/mol | H-TS | Osborn, Leahy, et al., 1998 | gas phase; B |
ΔrG° | 1565. ± 8.4 | kJ/mol | IMRE | Bartmess, Scott, et al., 1979 | gas phase; The acidity is 1.2 kcal/mol stronger than that from the D-EA cycle, due to the multi-compound fit for the acidity scale.; value altered from reference due to change in acidity scale; B |
ΔrG° | 1567. ± 8.8 | kJ/mol | H-TS | Haas and Harrison, 1993 | gas phase; Both metastable and 50 eV collision energy.; B |
ΔrG° | 1569.4 ± 2.5 | kJ/mol | TDEq | Meot-ner and Sieck, 1986 | gas phase; Experimental entropy: 21.5 eu, 0.6 less than H2O; B |
References
Go To: Top, Gas phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics data, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Rossini, 1932
Rossini, F.D.,
The heats of combustion of methyl and ethyl alcohols,
J. Res. NBS, 1932, 8, 119-139. [all data]
Thermodynamics Research Center, 1997
Thermodynamics Research Center,
Selected Values of Properties of Chemical Compounds., Thermodynamics Research Center, Texas A&M University, College Station, Texas, 1997. [all data]
Ivash E.V., 1955
Ivash E.V.,
Thermodynamic properties of ideal gaseous methanol,
J. Chem. Phys., 1955, 23, 1814-1818. [all data]
Zhuravlev E.Z., 1959
Zhuravlev E.Z.,
Isotopic effect on thermodynamic functions of some organic deuterocompounds in the ideal gas state,
Tr. Khim. i Khim. Tekhnol., 1959, 2, 475-485. [all data]
Chen S.S., 1977
Chen S.S.,
Thermodynamic properties of normal and deuterated methanols,
J. Phys. Chem. Ref. Data, 1977, 6, 105-112. [all data]
Chao J., 1986
Chao J.,
Ideal gas thermodynamic properties of simple alkanols,
Int. J. Thermophys., 1986, 7, 431-442. [all data]
Gurvich, Veyts, et al., 1989
Gurvich, L.V.; Veyts, I.V.; Alcock, C.B.,
Thermodynamic Properties of Individual Substances, 4th ed.; Vols. 1 and 2, Hemisphere, New York, 1989. [all data]
Chao J., 1986, 2
Chao J.,
Thermodynamic properties of key organic oxygen compounds in the carbon range C1 to C4. Part 2. Ideal gas properties,
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Stromsoe E., 1970
Stromsoe E.,
Heat capacity of alcohol vapors at atmospheric pressure,
J. Chem. Eng. Data, 1970, 15, 286-290. [all data]
Halford J.O., 1957
Halford J.O.,
Standard heat capacities of gaseous methanol, ethanol, methane and ethane at 279 K by thermal conductivity,
J. Phys. Chem., 1957, 61, 1536-1539. [all data]
De Vries T., 1941
De Vries T.,
The heat capacity of organic vapors. I. Methyl alcohol,
J. Am. Chem. Soc., 1941, 63, 1343-1346. [all data]
Weltner W., 1951
Weltner W., Jr.,
Methyl alcohol: the entropy, heat capacity and polymerization equilibria in the vapor, and potential barrier to internal rotation,
J. Am. Chem. Soc., 1951, 73, 2606-2610. [all data]
Gude and Teja, 1995
Gude, M.; Teja, A.S.,
Vapor-Liquid Critical Properties of Elements and Compounds. 4. Aliphatic Alkanols,
J. Chem. Eng. Data, 1995, 40, 1025-1036. [all data]
Craven and de Reuck, 1986
Craven, R.J.B.; de Reuck, K.M.,
Ideal-Gas and Saturation Properties of Methanol,
Int. J. Thermophys., 1986, 7, 541. [all data]
Francesconi, Lentz, et al., 1981
Francesconi, A.Z.; Lentz, H.; Franck, E.U.,
Phase Equilibriums and PVT Data for the Methane-Methanol System to 300 MPa and 240 degree C,
J. Phys. Chem., 1981, 85, 3303. [all data]
Zubarev and Bagdonas, 1969
Zubarev, V.N.; Bagdonas, A.,
Saturation Curve Properties and Specific Volumes of Methanol,
Teploenergetika (Moscow), 1969, 16, 88-91. [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]
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]
Yerlett and Wormald, 1986
Yerlett, T.K.; Wormald, C.J.,
The enthalpy of methanol,
The Journal of Chemical Thermodynamics, 1986, 18, 8, 719-726, https://doi.org/10.1016/0021-9614(86)90105-9
. [all data]
Cervenkova and Boublik, 1984
Cervenkova, Irena; Boublik, Tomas,
Vapor pressure, refractive indexes and densities at 20.0.degree.C, and vapor-liquid equilibrium at 101.325 kPa in the tert-amyl methyl ether-methanol system,
J. Chem. Eng. Data, 1984, 29, 4, 425-427, https://doi.org/10.1021/je00038a017
. [all data]
Gibbard and Creek, 1974
Gibbard, H. Frank; Creek, Jefferson L.,
Vapor pressure of methanol from 288.15 to 337.65.deg.K,
J. Chem. Eng. Data, 1974, 19, 4, 308-310, https://doi.org/10.1021/je60063a013
. [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]
Counsell and Lee, 1973
Counsell, J.F.; Lee, D.A.,
Thermodynamic properties of organic oxygen compounds 31. Vapour heat capacity and enthalpy of vaporization of methanol,
The Journal of Chemical Thermodynamics, 1973, 5, 4, 583-589, https://doi.org/10.1016/S0021-9614(73)80107-7
. [all data]
Svoboda, Veselý, et al., 1973
Svoboda, V.; Veselý, F.; Holub, R.; Pick, J.,
Enthalpy data of liquids. II. The dependence of heats of vaporization of methanol, propanol, butanol, cyclohexane, cyclohexene, and benzene on temperature,
Collect. Czech. Chem. Commun., 1973, 38, 12, 3539-3543, https://doi.org/10.1135/cccc19733539
. [all data]
Wilhoit and Zwolinski, 1973
Wilhoit, R.C.; Zwolinski, B.J.,
Physical and thermodynamic properties of aliphatic alcohols,
J. Phys. Chem. Ref. Data Suppl., 1973, 1, 2, 1. [all data]
Boublík and Aim, 1972
Boublík, T.; Aim, K.,
Heats of vaporization of simple non-spherical molecule compounds,
Collect. Czech. Chem. Commun., 1972, 37, 11, 3513-3521, https://doi.org/10.1135/cccc19723513
. [all data]
Ambrose and Sprake, 1970
Ambrose, D.; Sprake, C.H.S.,
Thermodynamic properties of organic oxygen compounds XXV. Vapour pressures and normal boiling temperatures of aliphatic alcohols,
The Journal of Chemical Thermodynamics, 1970, 2, 5, 631-645, https://doi.org/10.1016/0021-9614(70)90038-8
. [all data]
Hirata, Suda, et al., 1967
Hirata, Mitsuho; Suda, Seijiro; Onodera, Yutaka,
Vapor Pressure of Methanol in High Pressure Regions,
Chemical engineering, 1967, 31, 4, 339-342,a1, https://doi.org/10.1252/kakoronbunshu1953.31.339
. [all data]
Klyueva, Mischenko, et al., 1960
Klyueva, M.L.; Mischenko, K.P.; Fedorov, M.K.,
Zh. Prikl. Khim. (S.-Peterburg), 1960, 3, 473. [all data]
Ambrose, Sprake, et al., 1975
Ambrose, D.; Sprake, C.H.S.; Townsend, R.,
Thermodynamic Properties of Organic Oxygen Compounds. XXXVII. Vapour Pressures of Methanol, Ethanol, Pentan-1-ol, and Octan-1-ol from the Normal Boiling Temperature to the Critical Temperature,
J. Chem. Thermodyn., 1975, 7, 2, 185-190, https://doi.org/10.1016/0021-9614(75)90267-0
. [all data]
Hirata and Suda, 1967
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Notes
Go To: Top, Gas phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics data, References
- Symbols used in this document:
AE Appearance energy Cp,gas Constant pressure heat capacity of gas IE (evaluated) Recommended ionization energy Pc Critical pressure Tboil Boiling point Tc Critical temperature Tfus Fusion (melting) point Ttriple Triple point temperature Vc Critical volume d(ln(kH))/d(1/T) Temperature dependence parameter for Henry's Law constant k°H Henry's Law constant at 298.15K ΔHtrs Enthalpy of phase transition ΔStrs Entropy of phase transition ΔcH°gas Enthalpy of combustion of gas at standard conditions ΔfH°gas Enthalpy of formation of gas 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 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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