1-Propanol, 2-methyl-
- Formula: C4H10O
- Molecular weight: 74.1216
- IUPAC Standard InChIKey: ZXEKIIBDNHEJCQ-UHFFFAOYSA-N
- CAS Registry Number: 78-83-1
- 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. - Other names: Isobutyl alcohol; Isobutanol; Isopropylcarbinol; 2-Methyl-1-propanol; iso-C4H9OH; Fermentation butyl alcohol; 1-Hydroxymethylpropane; 2-Methylpropanol; 2-Methylpropan-1-ol; 2-Methylpropanol-1; 2-Methylpropyl alcohol; Butanol-iso; Alcool isobutylique; Isobutylalkohol; Rcra waste number U140; UN 1212; i-Butyl alcohol; Isopropyl carbitol; Propanol, 2-methyl-; 2-methyl-1-propanyl alcohol; i-Butanol; Methyl-2 propanol-1; NSC 5708; 2-methylpropanoI
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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
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
DRB - Donald R. Burgess, Jr.
DH - Eugene S. Domalski and Elizabeth D. Hearing
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 380.8 ± 0.9 | K | AVG | N/A | Average of 77 out of 89 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 165.15 | K | N/A | Anonymous, 1958 | TRC |
Tfus | 169. | K | N/A | Kanda, Otsubo, et al., 1950 | Uncertainty assigned by TRC = 2. K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 171.2 | K | N/A | Wilhoit, Chao, et al., 1985 | Uncertainty assigned by TRC = 0.01 K; TRC |
Ttriple | 171.18 | K | N/A | Counsell, Lees, et al., 1968 | Uncertainty assigned by TRC = 0.02 K; IPTS-48; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 548. ± 8. | K | AVG | N/A | Average of 10 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 45. ± 5. | bar | AVG | N/A | Average of 6 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Vc | 0.274 | l/mol | N/A | Gude and Teja, 1995 | |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 3.66 ± 0.02 | mol/l | N/A | Gude and Teja, 1995 | |
ρc | 3.672 | mol/l | N/A | Ambrose and Townsend, 1963 | TRC |
ρc | 3.63 | mol/l | N/A | Kay and Donham, 1955 | TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 51. ± 1. | kJ/mol | AVG | N/A | Average of 10 out of 11 values; Individual data points |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
41.82 | 381.1 | N/A | Majer and Svoboda, 1985 | |
45.4 | 365. | EB | Susial and Ortega, 1993 | Based on data from 350. to 400. K.; AC |
49.5 | 328. | A | Stephenson and Malanowski, 1987 | Based on data from 313. to 411. K.; AC |
46.0 | 396. | A | Stephenson and Malanowski, 1987 | Based on data from 381. to 524. K.; AC |
55.0 | 228. | A | Stephenson and Malanowski, 1987 | Based on data from 202. to 243. K.; AC |
44.2 | 379. | A | Stephenson and Malanowski, 1987 | Based on data from 369. to 389. K.; AC |
42.6 | 398. | A | Stephenson and Malanowski, 1987 | Based on data from 383. to 416. K.; AC |
41.1 | 416. | A | Stephenson and Malanowski, 1987 | Based on data from 401. to 493. K.; AC |
36.2 | 498. | A | Stephenson and Malanowski, 1987 | Based on data from 483. to 548. K.; AC |
46.2 | 357. | A,EB | Stephenson and Malanowski, 1987 | Based on data from 342. to 389. K. See also Ambrose, Counsell, et al., 1970.; AC |
49.7 ± 0.1 | 313. | C | Majer, Svoboda, et al., 1984 | AC |
48.3 ± 0.1 | 328. | C | Majer, Svoboda, et al., 1984 | AC |
45.0 ± 0.1 | 358. | C | Majer, Svoboda, et al., 1984 | AC |
48.1 | 335. | N/A | Sachek, Peshchenko, et al., 1982 | Based on data from 320. to 382. K.; AC |
52.6 | 308. | N/A | Wilhoit and Zwolinski, 1973 | Based on data from 293. to 388. K.; AC |
46.2 ± 0.1 | 347. | C | Counsell, Fenwick, et al., 1970 | AC |
44.2 ± 0.1 | 363. | C | Counsell, Fenwick, et al., 1970 | AC |
41.9 ± 0.1 | 381. | C | Counsell, Fenwick, et al., 1970 | AC |
47.0 | 348. | N/A | Brown, Fock, et al., 1969 | Based on data from 333. to 381. K. See also Boublik, Fried, et al., 1984.; AC |
40.1 | 438. | N/A | Ambrose and Townsend, 1963, 2 | Based on data from 423. to 548. K.; AC |
45.2 | 368. | EB | Biddiscombe, Collerson, et al., 1963 | Based on data from 353. to 388. K.; AC |
50.71 | 106.90 | V | Skinner and Snelson, 1960 | ALS |
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 381. |
---|---|
A (kJ/mol) | 49.05 |
α | -1.6587 |
β | 1.1038 |
Tc (K) | 547.7 |
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 |
---|---|---|---|---|---|
422.64 to 547.71 | 4.40062 | 1260.453 | -92.588 | Ambrose and Townsend, 1963, 3 | Coefficents calculated by NIST from author's data. |
353.36 to 388.77 | 4.43126 | 1236.991 | -101.528 | Biddiscombe, Collerson, et al., 1963, 2 | Coefficents calculated by NIST from author's data. |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
6.322 | 171.18 | Counsell, Lees, et al., 1968, 2 | DH |
6.32 | 171.2 | Counsell, Lees, et al., 1968 | AC |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
36.93 | 171.18 | Counsell, Lees, et al., 1968, 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.
Anonymous, 1958
Anonymous, X.,
Am. Pet. Inst. Res. Proj. 50, 1958, Unpublished, 1958. [all data]
Kanda, Otsubo, et al., 1950
Kanda, E.; Otsubo, A.; Haseda, T.,
Sci. Rep. Res. Inst., Tohoku Univ. Ser. A, 1950, 2, 9. [all data]
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]
Counsell, Lees, et al., 1968
Counsell, J.F.; Lees, E.B.; Martin, J.F.,
Thermodynamic properties of organic oxygen compounds. Part XIX. Low-temperature heat capacity and entropy of propan-1-ol, 2-methylpropan-1-ol, and pentan-1-ol,
J. Chem. Soc., A, 1968, 1819, https://doi.org/10.1039/j19680001819
. [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]
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]
Kay and Donham, 1955
Kay, W.B.; Donham, W.E.,
Liquid-Vapor Equilibrium in the Isobutyl Alcohol-Butanol, Methanol- Butanol, and Diethyl Ether-Butanol Systems,
Chem. Eng. Sci., 1955, 4, 1-16. [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]
Susial and Ortega, 1993
Susial, Pedro; Ortega, Juan,
Isobaric vapor-liquid equilibria for methyl propanoate + isobutyl alcohol,
J. Chem. Eng. Data, 1993, 38, 3, 434-436, https://doi.org/10.1021/je00011a028
. [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]
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]
Counsell, Fenwick, et al., 1970
Counsell, J.F.; Fenwick, J.O.; Lees, E.B.,
Thermodynamic properties of organic oxygen compounds 24. Vapour heat capacities and enthalpies of vaporization of ethanol, 2-methylpropan-1-ol, and pentan-1-ol,
The Journal of Chemical Thermodynamics, 1970, 2, 3, 367-372, https://doi.org/10.1016/0021-9614(70)90007-8
. [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]
Biddiscombe, Collerson, et al., 1963
Biddiscombe, D.P.; Collerson, R.R.; Handley, R.; Herington, E.F.G.; Martin, J.F.; Sprake, C.H.S.,
364. Thermodynamic properties of organic oxygen compounds. Part VIII. Purification and vapour pressures of the propyl and butyl alcohols,
J. Chem. Soc., 1963, 1954, https://doi.org/10.1039/jr9630001954
. [all data]
Skinner and Snelson, 1960
Skinner, H.A.; Snelson, A.,
The heats of combustion of the four isomeric butyl alcohols,
Trans. Faraday Soc., 1960, 56, 1776-1783. [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, 2
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]
Counsell, Lees, et al., 1968, 2
Counsell, J.F.; Lees, E.B.; Martin, J.F.,
Thermodynamic properties of organic oxygen compounds. Part XIX. Low temperature heat capacity and entropy of propan-1-ol, 2-methyl-propan-1-ol,
and pentan-1-ol, 1968, J. [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 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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