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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Gas phase thermochemistry data
Go To: Top, Phase change data, Gas phase ion energetics 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:
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 | -312.6 ± 0.88 | kJ/mol | Eqk | Wiberg and Hao, 1991 | Heat of hydration; ALS |
ΔfH°gas | -313. ± 1.5 | kJ/mol | Ccb | Skinner and Snelson, 1960 | ALS |
ΔfH°gas | -309.7 | kJ/mol | N/A | Taft and Riesz, 1955 | Value 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 |
---|---|---|---|
35.85 | 50. | Thermodynamics Research Center, 1997 | p=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 |
52.73 | 100. | ||
70.40 | 150. | ||
85.29 | 200. | ||
106.29 | 273.15 | ||
113.63 ± 0.21 | 298.15 | ||
114.18 | 300. | ||
142.99 | 400. | ||
168.39 | 500. | ||
189.65 | 600. | ||
207.49 | 700. | ||
222.71 | 800. | ||
235.85 | 900. | ||
247.26 | 1000. | ||
257.20 | 1100. | ||
265.85 | 1200. | ||
273.37 | 1300. | ||
279.92 | 1400. | ||
285.62 | 1500. | ||
296.9 | 1750. | ||
304.9 | 2000. | ||
310.7 | 2250. | ||
314.9 | 2500. | ||
318.0 | 2750. | ||
320.3 | 3000. |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
133.4 ± 1.1 | 360.55 | Stromsoe E., 1970 | 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 1.13 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 |
132.63 | 365.15 | ||
136.2 ± 1.1 | 372.85 | ||
137.95 | 383.15 | ||
139.2 ± 1.1 | 385.65 | ||
142.88 | 401.15 | ||
145.1 ± 1.1 | 410.85 | ||
148.07 | 419.15 | ||
153.55 | 437.15 | ||
151.9 ± 1.1 | 439.85 | ||
152.2 ± 1.1 | 441.45 | ||
159.1 ± 1.1 | 470.75 | ||
165.7 ± 1.1 | 499.25 | ||
172.6 ± 1.1 | 528.75 | ||
183.4 ± 1.1 | 575.05 | ||
187.3 ± 1.1 | 591.55 |
Phase change data
Go To: Top, Gas phase thermochemistry data, Gas phase ion energetics 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 |
---|---|---|---|---|---|
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)
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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)
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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 |
Gas phase ion energetics data
Go To: Top, Gas phase thermochemistry data, Phase change 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 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
LLK - Sharon G. Lias, Rhoda D. Levin, and Sherif A. Kafafi
RDSH - Henry M. Rosenstock, Keith Draxl, Bruce W. Steiner, and John T. Herron
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
IE (evaluated) | 9.90 ± 0.03 | eV | N/A | N/A | L |
Quantity | Value | Units | Method | Reference | Comment |
Proton affinity (review) | 802.6 | kJ/mol | N/A | Hunter and Lias, 1998 | HL |
Quantity | Value | Units | Method | Reference | Comment |
Gas basicity | 772.2 | kJ/mol | N/A | Hunter and Lias, 1998 | HL |
Ionization energy determinations
IE (eV) | Method | Reference | Comment |
---|---|---|---|
9.90 ± 0.03 | PIPECO | Shao, Baer, et al., 1988 | LL |
9.97 ± 0.02 | PE | Cocksey, Eland, et al., 1971 | LLK |
10.23 | PE | Baker, Betteridge, et al., 1971 | LLK |
10.23 | PE | Baker, Betteridge, et al., 1971 | LLK |
10.26 | PE | Benoit and Harrison, 1977 | Vertical value; LLK |
10.25 ± 0.03 | PE | Peel and Willett, 1975 | Vertical value; LLK |
10.25 | PE | Robin and Kuebler, 1973 | Vertical value; LLK |
Appearance energy determinations
Ion | AE (eV) | Other Products | Method | Reference | Comment |
---|---|---|---|---|---|
C3H7O+ | 9.86 | CH3 | EI | Lossing, 1977 | LLK |
C3H7O+ | 10.1 ± 0.2 | CH3 | EI | Beauchamp, Caserio, et al., 1974 | LLK |
C3H7O+ | 9.87 ± 0.03 | CH3 | PI | Potapov and Sorokin, 1972 | LLK |
C3H7O+ | 9.87 | CH3 | EI | Potapov and Sorokin, 1970 | RDSH |
C3H7O+ | 10.2 | CH3 | EI | Harrison, Ivko, et al., 1966 | RDSH |
De-protonation reactions
C4H9O- + =
By formula: C4H9O- + H+ = C4H10O
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1568. ± 4.2 | kJ/mol | D-EA | Ramond, Davico, et al., 2000 | gas phase; B |
ΔrH° | 1567. ± 8.8 | kJ/mol | G+TS | Bartmess, Scott, et al., 1979 | gas phase; value altered from reference due to change in acidity scale; B |
ΔrH° | 1573.2 ± 2.9 | kJ/mol | CIDT | DeTuri and Ervin, 1999 | gas phase; B |
ΔrH° | 1566. ± 8.4 | kJ/mol | CIDC | Haas and Harrison, 1993 | gas phase; Both metastable and 50 eV collision energy.; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1540. ± 4.6 | kJ/mol | H-TS | Ramond, Davico, et al., 2000 | gas phase; B |
ΔrG° | 1540. ± 8.4 | kJ/mol | IMRE | Bartmess, Scott, et al., 1979 | gas phase; value altered from reference due to change in acidity scale; B |
ΔrG° | 1538. ± 8.8 | kJ/mol | H-TS | Haas and Harrison, 1993 | gas phase; Both metastable and 50 eV collision energy.; B |
Mass spectrum (electron ionization)
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: NIST Mass Spectrometry Data Center, William E. Wallace, director
Spectrum
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Additional Data
View image of digitized spectrum (can be printed in landscape orientation).
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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 |
References
Go To: Top, Gas phase thermochemistry data, Phase change data, Gas phase ion energetics 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,
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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,
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Oetting, 1963
Oetting, F.L.,
The heat capacity and entropy of 2-methyl-2-propanol from 15 to 330!31k,
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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,
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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,
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. [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
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Notes
Go To: Top, Gas phase thermochemistry data, Phase change data, Gas phase ion energetics data, Mass spectrum (electron ionization), 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 ΔHtrs Enthalpy of phase transition ΔStrs Entropy of phase transition 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 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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