2-Propanol, 2-methyl-
- Formula: C4H10O
- Molecular weight: 74.1216
- IUPAC Standard InChIKey: DKGAVHZHDRPRBM-UHFFFAOYSA-N
- CAS Registry Number: 75-65-0
- 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: tert-Butyl alcohol; tert-Butanol; Ethanol, 1,1-Dimethyl-; Trimethylcarbinol; Trimethylmethanol; 1,1-Dimethylethanol; 2-Methyl-2-propanol; tert-C4H9OH; t-Butanol; tert-Butyl hydroxide; 2-Methylpropanol-2; 2-Methylpropan-2-ol; Alcool butylique tertiaire; Butanol tertiaire; t-Butyl hydroxide; Methanol, trimethyl-; NCI-C55367; 2-Methyl n-propan-2-ol; Methyl-2 propanol-2; Tert.-butyl alcohol
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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
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
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 | 355.5 ± 0.7 | K | AVG | N/A | Average of 65 out of 70 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 298.3 ± 0.7 | K | AVG | N/A | Average of 15 out of 17 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 298.96 | K | N/A | Wilhoit, Chao, et al., 1985 | Crystal phase 1 phase; Uncertainty assigned by TRC = 0.06 K; TRC |
Ttriple | 298.97 | K | N/A | Oetting, 1963 | Crystal phase 1 phase; Uncertainty assigned by TRC = 0.06 K; TRC |
Ttriple | 298.5 | K | N/A | Parks and Anderson, 1926 | Uncertainty assigned by TRC = 0.2 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 506.2 ± 0.3 | K | N/A | Gude and Teja, 1995 | |
Tc | 506.2 | K | N/A | Majer and Svoboda, 1985 | |
Tc | 506.2 | K | N/A | Ambrose and Townsend, 1963 | TRC |
Tc | 508.9 | K | N/A | Krone and Johnson, 1956 | TRC |
Tc | 508.1 | K | N/A | Pawlewski, 1883 | TRC |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 39.7 ± 0.2 | bar | N/A | Gude and Teja, 1995 | |
Pc | 39.72 | bar | N/A | Ambrose and Townsend, 1963 | TRC |
Pc | 42.32 | bar | N/A | Krone and Johnson, 1956 | TRC |
Quantity | Value | Units | Method | Reference | Comment |
Vc | 0.275 | l/mol | N/A | Gude and Teja, 1995 | |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 3.64 ± 0.02 | mol/l | N/A | Gude and Teja, 1995 | |
ρc | 3.643 | mol/l | N/A | Ambrose and Townsend, 1963 | TRC |
ρc | 3.48 | mol/l | N/A | Krone and Johnson, 1956 | TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 46. ± 1. | kJ/mol | AVG | N/A | Average of 11 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ΔsubH° | 41. | kJ/mol | V | Raley, Rust, et al., 1948 | ALS |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
39.07 | 355.5 | N/A | Majer and Svoboda, 1985 | |
42.7 | 338. | N/A | Ortega, Espiau, et al., 2003 | Based on data from 323. to 368. K.; AC |
43.4 | 336. | N/A | Aucejo, Loras, et al., 1999 | Based on data from 321. to 359. K.; AC |
46.2 | 314. | A | Stephenson and Malanowski, 1987 | Based on data from 299. to 375. K.; AC |
41.4 | 355. | A | Stephenson and Malanowski, 1987 | Based on data from 347. to 363. K.; AC |
43.2 | 371. | A | Stephenson and Malanowski, 1987 | Based on data from 356. to 480. K.; AC |
41.4 | 355. | A | Stephenson and Malanowski, 1987 | Based on data from 347. to 363. K.; AC |
39.8 | 372. | A | Stephenson and Malanowski, 1987 | Based on data from 357. to 461. K.; AC |
33.6 | 468. | A | Stephenson and Malanowski, 1987 | Based on data from 453. to 506. K.; AC |
42.6 | 344. | EB | Stephenson and Malanowski, 1987 | Based on data from 329. to 363. K. See also Ambrose, Counsell, et al., 1970 and Beynon and McKetta, 1963.; AC |
46.12 ± 0.05 | 303.2 | C | Majer, Svoboda, et al., 1984 | ALS |
46.2 ± 0.1 | 303. | C | Majer, Svoboda, et al., 1984 | AC |
44.9 ± 0.1 | 313. | C | Majer, Svoboda, et al., 1984 | AC |
43.0 ± 0.1 | 328. | C | Majer, Svoboda, et al., 1984 | AC |
41.0 ± 0.1 | 343. | C | Majer, Svoboda, et al., 1984 | AC |
37.2 ± 0.1 | 368. | C | Majer, Svoboda, et al., 1984 | AC |
44.7 | 321. | N/A | Sachek, Peshchenko, et al., 1982 | Based on data from 306. to 357. K.; AC |
46.5 | 308. | N/A | Wilhoit and Zwolinski, 1973 | Based on data from 293. to 376. K.; AC |
44.2 | 328. | N/A | Brown, Fock, et al., 1969 | Based on data from 313. to 355. K. See also Boublik, Fried, et al., 1984.; AC |
38.7 | 388. | N/A | Ambrose and Townsend, 1963, 2 | Based on data from 373. to 506. K.; AC |
42.1 | 348. | EB | Beynon and McKetta, 1963 | Based on data from 333. to 363. K.; AC |
42.5 ± 0.1 | 330. | C | Beynon and McKetta, 1963 | AC |
41.3 ± 0.1 | 340. | C | Beynon and McKetta, 1963 | AC |
40.4 ± 0.1 | 346. | C | Beynon and McKetta, 1963 | AC |
40.0 ± 0.1 | 349. | C | Beynon and McKetta, 1963 | AC |
39.0 ± 0.1 | 356. | C | Beynon and McKetta, 1963 | AC |
44.7 | 323. | N/A | Parks and Barton, 1928 | Based on data from 293. to 363. 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)
View plot Requires a JavaScript / HTML 5 canvas capable browser.
Temperature (K) | 298. to 385. |
---|---|
A (kJ/mol) | 69.08 |
α | -0.3583 |
β | 0.678 |
Tc (K) | 506.2 |
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 |
---|---|---|---|---|---|
312.66 to 355.56 | 4.49774 | 1174.869 | -93.92 | Brown, Fock, et al., 1969 | Coefficents calculated by NIST from author's data. |
376.42 to 506. | 4.26383 | 1075.578 | -102.588 | Ambrose and Townsend, 1963, 3 | Coefficents calculated by NIST from author's data. |
330.6 to 363. | 4.59323 | 1225.649 | -88.316 | Beynon and McKetta, 1963 | Coefficents calculated by NIST from author's data. |
333.93 to 362.71 | 4.33258 | 1095.084 | -102.409 | Biddiscombe, Collerson, et al., 1963 | Coefficents calculated by NIST from author's data. |
Enthalpy of sublimation
ΔsubH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
51.3 | 275. | A | Stull, 1947 | Based on data from 253. to 298. K.; AC |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
6.7 | 299. | Domalski and Hearing, 1996 | AC |
6.782 | 298.5 | Parks and Anderson, 1926, 2 | DH |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
22.72 | 298.5 | Parks and Anderson, 1926, 2 | DH |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
2.9 | 286.1 | Domalski and Hearing, 1996 | CAL |
1.66 | 294.5 | ||
22.42 | 299.0 |
Enthalpy of phase transition
ΔHtrs (kJ/mol) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
0.828 | 286.14 | crystaline, II | crystaline, I | Oetting F.L., 1963 | DH |
0.490 | 294.47 | crystaline, III | crystaline, I | Oetting F.L., 1963 | Metastable transition, not always reproducible, c,III,metastable form.; DH |
6.7028 | 298.97 | crystaline, I | liquid | Oetting F.L., 1963 | DH |
Entropy of phase transition
ΔStrs (J/mol*K) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
2.89 | 286.14 | crystaline, II | crystaline, I | Oetting F.L., 1963 | DH |
1.66 | 294.47 | crystaline, III | crystaline, I | Oetting F.L., 1963 | Metastable; DH |
22.42 | 298.97 | crystaline, I | liquid | Oetting F.L., 1963 | 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.
Wilhoit, Chao, et al., 1985
Wilhoit, R.C.; Chao, J.; Hall, K.R.,
Thermodynamic Properties of Key Organic Compounds in the Carbon Range C1 to C4. Part 1. Properties of Condensed Phases,
J. Phys. Chem. Ref. Data, 1985, 14, 1. [all data]
Oetting, 1963
Oetting, F.L.,
The heat capacity and entropy of 2-methyl-2-propanol from 15 to 330!31k,
J. Phys. Chem., 1963, 67, 2757-61. [all data]
Parks and Anderson, 1926
Parks, G.S.; Anderson, C.T.,
Thermal data on organic compounds. III. The heat capacities, entropies and free energies of tertiary butyl alcohol, mannitol, erythritol and normal butyric acid,
J. Am. Chem. Soc., 1926, 48, 1506-12. [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]
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]
Ambrose and Townsend, 1963
Ambrose, D.; Townsend, R.,
Thermodynamic Properties of Organic Oxygen Compounds IX. The Critical Properties and Vapor Pressures Above Five Atmospheres of Six Aliphatic Alcohols,
J. Chem. Soc., 1963, 54, 3614-25. [all data]
Krone and Johnson, 1956
Krone, L.H.; Johnson, R.C.,
Thermodynamic Properties of tert-Butyl ALcohol,
AIChE J., 1956, 2, 552-4. [all data]
Pawlewski, 1883
Pawlewski, B.,
Critical temperatures of some liquids,
Ber. Dtsch. Chem. Ges., 1883, 16, 2633-36. [all data]
Raley, Rust, et al., 1948
Raley, J.H.; Rust, F.F.; Vaughan, W.E.,
Decompositions of Di-t-alkyl peroxides. I. Kinetics,
J. Am. Chem. Soc., 1948, 70, 88-94. [all data]
Ortega, Espiau, et al., 2003
Ortega, Juan; Espiau, Fernando; Postigo, Miguel,
Isobaric Vapor-Liquid Equilibria and Excess Quantities for Binary Mixtures of an Ethyl Ester + tert -Butanol and a New Approach to VLE Data Processing,
J. Chem. Eng. Data, 2003, 48, 4, 916-924, https://doi.org/10.1021/je0202073
. [all data]
Aucejo, Loras, et al., 1999
Aucejo, Antonio; Loras, Sonia; Muñoz, Rosa; Ordoñez, Luis Miguel,
Isobaric vapor--liquid equilibrium for binary mixtures of 2-methylpentane+ethanol and +2-methyl-2-propanol,
Fluid Phase Equilibria, 1999, 156, 1-2, 173-183, https://doi.org/10.1016/S0378-3812(99)00029-1
. [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]
Ambrose, Counsell, et al., 1970
Ambrose, D.; Counsell, J.F.; Davenport, A.J.,
The use of Chebyshev polynomials for the representation of vapour pressures between the triple point and the critical point,
The Journal of Chemical Thermodynamics, 1970, 2, 2, 283-294, https://doi.org/10.1016/0021-9614(70)90093-5
. [all data]
Beynon and McKetta, 1963
Beynon, Eugene T.; McKetta, John J.,
THE THERMODYNAMIC PROPERTIES OF 2-METHYL-2-PROPANOL,
J. Phys. Chem., 1963, 67, 12, 2761-2765, https://doi.org/10.1021/j100806a060
. [all data]
Majer, Svoboda, et al., 1984
Majer, V.; Svoboda, V.; Hynek, V.,
On the enthalpy of vaporization of isomeric butanols,
J. Chem. Thermodyn., 1984, 16, 1059-1066. [all data]
Sachek, Peshchenko, et al., 1982
Sachek, A.I.; Peshchenko, A.D.; Markovnik, V.S.; Ral'ko, O.V.; Andreevskii, D.N.; Leont'eva, A.A.,
Termodin. Org. Soedin., 1982, 94. [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]
Brown, Fock, et al., 1969
Brown, I.; Fock, W.; Smith, F.,
The thermodynamic properties of solutions of normal and branched alcohols in benzene and n-hexane,
The Journal of Chemical Thermodynamics, 1969, 1, 3, 273-291, https://doi.org/10.1016/0021-9614(69)90047-0
. [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]
Ambrose and Townsend, 1963, 2
Ambrose, D.; Townsend, R.,
681. Thermodynamic properties of organic oxygen compounds. Part IX. The critical properties and vapour pressures, above five atmospheres, of six aliphatic alcohols,
J. Chem. Soc., 1963, 3614, https://doi.org/10.1039/jr9630003614
. [all data]
Parks and Barton, 1928
Parks, George S.; Barton, Bernard,
VAPOR PRESSURE DATA FOR ISOPROPYL ALCOHOL AND TERTIARY BUTYL ALCOHOL,
J. Am. Chem. Soc., 1928, 50, 1, 24-26, https://doi.org/10.1021/ja01388a004
. [all data]
Ambrose and Townsend, 1963, 3
Ambrose, D.; Townsend, R.,
Thermodynamic Properties of Organic Oxygen Compounds. Part 9. The Critical Properties and Vapour Pressures, above Five Atmospheres, of Six Aliphatic Alcohols,
J. Chem. Soc., 1963, 3614-3625, https://doi.org/10.1039/jr9630003614
. [all data]
Biddiscombe, Collerson, et al., 1963
Biddiscombe, D.P.; Collerson, R.R.; Handley, R.; Herington, E.F.G.; Martin, J.F.; Sprake, C.H.S.,
Thermodynamic Properties of Organic Oxygen Compounds. Part 8. Purification and Vapor Pressures of the Propyl and Butyl Alcohols,
J. Chem. Soc., 1963, 1954-1957, https://doi.org/10.1039/jr9630001954
. [all data]
Stull, 1947
Stull, Daniel R.,
Vapor Pressure of Pure Substances. Organic and Inorganic Compounds,
Ind. Eng. Chem., 1947, 39, 4, 517-540, https://doi.org/10.1021/ie50448a022
. [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]
Parks and Anderson, 1926, 2
Parks, G.S.; Anderson, C.T.,
Thermal data on organic compounds. III. The heat capacities, entropies and free energies of tertiary butyl alcohol, mannitol, erythritol and normal butyric acid,
J. Am. Chem. Soc., 1926, 48, 1506-1512. [all data]
Oetting F.L., 1963
Oetting F.L.,
The heat capacity and entropy of 2-methyl-2-propanol from 15 to 330 K,
J. Phys. Chem., 1963, 67, 2757-2761. [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 ΔHtrs Enthalpy of phase transition ΔStrs Entropy of phase transition ΔfusH Enthalpy of fusion ΔfusS Entropy of fusion ΔsubH Enthalpy of sublimation 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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