2-Propanol, 2-methyl-

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Gas phase thermochemistry 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:
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
Δfgas-312.6 ± 0.88kJ/molEqkWiberg and Hao, 1991Heat of hydration; ALS
Δfgas-313. ± 1.5kJ/molCcbSkinner and Snelson, 1960ALS
Δfgas-309.7kJ/molN/ATaft and Riesz, 1955Value computed using ΔfHliquid° value of -356.0 kj/mol from Taft and Riesz, 1955 and ΔvapH° value of 46.3 kj/mol from Skinner and Snelson, 1960.; DRB

Constant pressure heat capacity of gas

Cp,gas (J/mol*K) Temperature (K) Reference Comment
35.8550.Thermodynamics Research Center, 1997p=1 bar. Selected values of S(T) and Cp(T) are in good agreement with those of [ Beynon E.T., 1963] because of using practically the same molecular constants in two calculations. Please also see Chao J., 1986.; GT
52.73100.
70.40150.
85.29200.
106.29273.15
113.63 ± 0.21298.15
114.18300.
142.99400.
168.39500.
189.65600.
207.49700.
222.71800.
235.85900.
247.261000.
257.201100.
265.851200.
273.371300.
279.921400.
285.621500.
296.91750.
304.92000.
310.72250.
314.92500.
318.02750.
320.33000.

Constant pressure heat capacity of gas

Cp,gas (J/mol*K) Temperature (K) Reference Comment
133.4 ± 1.1360.55Stromsoe E., 1970Ideal 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 1.13 J/mol*K. The accuracy of the experimental heat capacities [ Stromsoe E., 1970] is estimated as less than 0.3%. Please also see Beynon E.T., 1963.; GT
132.63365.15
136.2 ± 1.1372.85
137.95383.15
139.2 ± 1.1385.65
142.88401.15
145.1 ± 1.1410.85
148.07419.15
153.55437.15
151.9 ± 1.1439.85
152.2 ± 1.1441.45
159.1 ± 1.1470.75
165.7 ± 1.1499.25
172.6 ± 1.1528.75
183.4 ± 1.1575.05
187.3 ± 1.1591.55

Phase change data

Go To: Top, Gas phase thermochemistry data, Mass spectrum (electron ionization), 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
Tboil355.5 ± 0.7KAVGN/AAverage of 65 out of 70 values; Individual data points
Quantity Value Units Method Reference Comment
Tfus298.3 ± 0.7KAVGN/AAverage of 15 out of 17 values; Individual data points
Quantity Value Units Method Reference Comment
Ttriple298.96KN/AWilhoit, Chao, et al., 1985Crystal phase 1 phase; Uncertainty assigned by TRC = 0.06 K; TRC
Ttriple298.97KN/AOetting, 1963Crystal phase 1 phase; Uncertainty assigned by TRC = 0.06 K; TRC
Ttriple298.5KN/AParks and Anderson, 1926Uncertainty assigned by TRC = 0.2 K; TRC
Quantity Value Units Method Reference Comment
Tc506.2 ± 0.3KN/AGude and Teja, 1995 
Tc506.2KN/AMajer and Svoboda, 1985 
Tc506.2KN/AAmbrose and Townsend, 1963TRC
Tc508.9KN/AKrone and Johnson, 1956TRC
Tc508.1KN/APawlewski, 1883TRC
Quantity Value Units Method Reference Comment
Pc39.7 ± 0.2barN/AGude and Teja, 1995 
Pc39.72barN/AAmbrose and Townsend, 1963TRC
Pc42.32barN/AKrone and Johnson, 1956TRC
Quantity Value Units Method Reference Comment
Vc0.275l/molN/AGude and Teja, 1995 
Quantity Value Units Method Reference Comment
ρc3.64 ± 0.02mol/lN/AGude and Teja, 1995 
ρc3.643mol/lN/AAmbrose and Townsend, 1963TRC
ρc3.48mol/lN/AKrone and Johnson, 1956TRC
Quantity Value Units Method Reference Comment
Δvap46. ± 1.kJ/molAVGN/AAverage of 11 values; Individual data points
Quantity Value Units Method Reference Comment
Δsub41.kJ/molVRaley, Rust, et al., 1948ALS

Enthalpy of vaporization

ΔvapH (kJ/mol) Temperature (K) Method Reference Comment
39.07355.5N/AMajer and Svoboda, 1985 
42.7338.N/AOrtega, Espiau, et al., 2003Based on data from 323. to 368. K.; AC
43.4336.N/AAucejo, Loras, et al., 1999Based on data from 321. to 359. K.; AC
46.2314.AStephenson and Malanowski, 1987Based on data from 299. to 375. K.; AC
41.4355.AStephenson and Malanowski, 1987Based on data from 347. to 363. K.; AC
43.2371.AStephenson and Malanowski, 1987Based on data from 356. to 480. K.; AC
41.4355.AStephenson and Malanowski, 1987Based on data from 347. to 363. K.; AC
39.8372.AStephenson and Malanowski, 1987Based on data from 357. to 461. K.; AC
33.6468.AStephenson and Malanowski, 1987Based on data from 453. to 506. K.; AC
42.6344.EBStephenson and Malanowski, 1987Based on data from 329. to 363. K. See also Ambrose, Counsell, et al., 1970 and Beynon and McKetta, 1963.; AC
46.12 ± 0.05303.2CMajer, Svoboda, et al., 1984ALS
46.2 ± 0.1303.CMajer, Svoboda, et al., 1984AC
44.9 ± 0.1313.CMajer, Svoboda, et al., 1984AC
43.0 ± 0.1328.CMajer, Svoboda, et al., 1984AC
41.0 ± 0.1343.CMajer, Svoboda, et al., 1984AC
37.2 ± 0.1368.CMajer, Svoboda, et al., 1984AC
44.7321.N/ASachek, Peshchenko, et al., 1982Based on data from 306. to 357. K.; AC
46.5308.N/AWilhoit and Zwolinski, 1973Based on data from 293. to 376. K.; AC
44.2328.N/ABrown, Fock, et al., 1969Based on data from 313. to 355. K. See also Boublik, Fried, et al., 1984.; AC
38.7388.N/AAmbrose and Townsend, 1963, 2Based on data from 373. to 506. K.; AC
42.1348.EBBeynon and McKetta, 1963Based on data from 333. to 363. K.; AC
42.5 ± 0.1330.CBeynon and McKetta, 1963AC
41.3 ± 0.1340.CBeynon and McKetta, 1963AC
40.4 ± 0.1346.CBeynon and McKetta, 1963AC
40.0 ± 0.1349.CBeynon and McKetta, 1963AC
39.0 ± 0.1356.CBeynon and McKetta, 1963AC
44.7323.N/AParks and Barton, 1928Based 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)

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Temperature (K) 298. to 385.
A (kJ/mol) 69.08
α -0.3583
β 0.678
Tc (K) 506.2
ReferenceMajer and Svoboda, 1985

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
312.66 to 355.564.497741174.869-93.92Brown, Fock, et al., 1969Coefficents calculated by NIST from author's data.
376.42 to 506.4.263831075.578-102.588Ambrose and Townsend, 1963, 3Coefficents calculated by NIST from author's data.
330.6 to 363.4.593231225.649-88.316Beynon and McKetta, 1963Coefficents calculated by NIST from author's data.
333.93 to 362.714.332581095.084-102.409Biddiscombe, Collerson, et al., 1963Coefficents calculated by NIST from author's data.

Enthalpy of sublimation

ΔsubH (kJ/mol) Temperature (K) Method Reference Comment
51.3275.AStull, 1947Based on data from 253. to 298. K.; AC

Enthalpy of fusion

ΔfusH (kJ/mol) Temperature (K) Reference Comment
6.7299.Domalski and Hearing, 1996AC
6.782298.5Parks and Anderson, 1926, 2DH

Entropy of fusion

ΔfusS (J/mol*K) Temperature (K) Reference Comment
22.72298.5Parks and Anderson, 1926, 2DH

Entropy of fusion

ΔfusS (J/mol*K) Temperature (K) Reference Comment
2.9286.1Domalski and Hearing, 1996CAL
1.66294.5
22.42299.0

Enthalpy of phase transition

ΔHtrs (kJ/mol) Temperature (K) Initial Phase Final Phase Reference Comment
0.828286.14crystaline, IIcrystaline, IOetting F.L., 1963DH
0.490294.47crystaline, IIIcrystaline, IOetting F.L., 1963Metastable transition, not always reproducible, c,III,metastable form.; DH
6.7028298.97crystaline, IliquidOetting F.L., 1963DH

Entropy of phase transition

ΔStrs (J/mol*K) Temperature (K) Initial Phase Final Phase Reference Comment
2.89286.14crystaline, IIcrystaline, IOetting F.L., 1963DH
1.66294.47crystaline, IIIcrystaline, IOetting F.L., 1963Metastable; DH
22.42298.97crystaline, IliquidOetting F.L., 1963DH

In addition to the Thermodynamics Research Center (TRC) data available from this site, much more physical and chemical property data is available from the following TRC products:


Mass spectrum (electron ionization)

Go To: Top, Gas phase thermochemistry data, 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 by: NIST Mass Spectrometry Data Center, William E. Wallace, director

Spectrum

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Mass spectrum
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Additional Data

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Owner NIST Mass Spectrometry Data Center
Collection (C) 2014 copyright by the U.S. Secretary of Commerce
on behalf of the United States of America. All rights reserved.
Origin NIST Mass Spectrometry Data Center, 1998.
NIST MS number 291339

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References

Go To: Top, Gas phase thermochemistry data, Phase change data, Mass spectrum (electron ionization), Notes

Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.

Wiberg and Hao, 1991
Wiberg, K.B.; Hao, S., Enthalpies of hydration of alkenes. 4. Formation of acyclic tert-alcohols, J. Org. Chem., 1991, 56, 5108-5110. [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]

Taft and Riesz, 1955
Taft, R.W., Jr.; Riesz, P., Thermodynamic properties for the system isobutene-t-butyl alcohol, J. Am. Chem. Soc., 1955, 77, 902-904. [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]

Beynon E.T., 1963
Beynon E.T., Jr., The thermodynamic properties of 2-methyl-2-propanol, J. Phys. Chem., 1963, 67, 2761-2765. [all data]

Chao J., 1986
Chao J., Thermodynamic properties of key organic oxygen compounds in the carbon range C1 to C4. Part 2. Ideal gas properties, J. Phys. Chem. Ref. Data, 1986, 15, 1369-1436. [all data]

Stromsoe E., 1970
Stromsoe E., Heat capacity of alcohol vapors at atmospheric pressure, J. Chem. Eng. Data, 1970, 15, 286-290. [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]

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, Gas phase thermochemistry data, Phase change data, Mass spectrum (electron ionization), References