1-Butanol
- Formula: C4H10O
- Molecular weight: 74.1216
- IUPAC Standard InChIKey: LRHPLDYGYMQRHN-UHFFFAOYSA-N
- CAS Registry Number: 71-36-3
- 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: Butyl alcohol; n-Butan-1-ol; n-Butanol; n-Butyl alcohol; Butyl hydroxide; CCS 203; Hemostyp; Methylolpropane; Propylcarbinol; n-C4H9OH; Butanol; Butan-1-ol; 1-Hydroxybutane; Alcool butylique; Butanolo; Butylowy alkohol; Butyric alcohol; Propylmethanol; Butanolen; 1-Butyl alcohol; Rcra waste number U031; Butanol-1; NSC 62782
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Gas phase thermochemistry data
Go To: Top, 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 compiled as indicated in comments:
DRB - Donald R. Burgess, Jr.
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
GT - Glushko Thermocenter, Russian Academy of Sciences, Moscow
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°gas | -277. ± 5. | kJ/mol | AVG | N/A | Average of 13 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
S°gas | 361.98 | J/mol*K | N/A | Chao J., 1986 | Other values of S(298.15 K) based on low-temperature thermal measurements are (in J/mol*K): 363.17 [65COU/HAL], 362.33 [ Chermin H.A.G., 1961], and 361.9 [ Buckley E., 1967].; GT |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
42.54 | 50. | Thermodynamics Research Center, 1997 | p=1 bar. Recommended S(T) and Cp(T) values agree with those calculated by [ Chermin H.A.G., 1961] within 1.5 J/mol*K. S(T) values calculated by [ Dyatkina M.E., 1954] are different from values given here by 12-30 J/mol*K. Please also see Chao J., 1986.; GT |
58.33 | 100. | ||
70.10 | 150. | ||
81.28 | 200. | ||
100.68 | 273.15 | ||
108.03 ± 0.25 | 298.15 | ||
108.58 | 300. | ||
138.16 | 400. | ||
164.42 | 500. | ||
186.38 | 600. | ||
204.83 | 700. | ||
220.56 | 800. | ||
234.15 | 900. | ||
245.93 | 1000. | ||
256.18 | 1100. | ||
265.10 | 1200. | ||
272.86 | 1300. | ||
279.63 | 1400. | ||
285.54 | 1500. | ||
297.3 | 1750. | ||
305.8 | 2000. | ||
312.2 | 2250. | ||
316.9 | 2500. | ||
320.5 | 2750. | ||
323.2 | 3000. |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
140.93 ± 0.79 | 395.25 | 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 0.79 J/mol*K. The accuracy of the experimental heat capacities [ Stromsoe E., 1970] is estimated as less than 0.3%.; GT |
137.88 | 398.15 | ||
143.00 ± 0.79 | 404.15 | ||
144.16 ± 0.79 | 409.15 | ||
142.06 | 413.15 | ||
146.58 ± 0.79 | 419.55 | ||
149.26 ± 0.79 | 431.05 | ||
147.42 | 433.15 | ||
151.60 ± 0.79 | 441.15 | ||
152.66 | 453.15 | ||
155.88 ± 0.79 | 459.55 | ||
162.55 ± 0.79 | 488.25 | ||
169.95 ± 0.79 | 520.05 | ||
175.97 ± 0.79 | 545.95 | ||
181.20 ± 0.79 | 568.45 | ||
189.31 ± 0.79 | 603.35 |
Phase change data
Go To: Top, Gas phase thermochemistry 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 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 | 390.6 ± 0.8 | K | AVG | N/A | Average of 137 out of 146 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 188. ± 9. | K | AVG | N/A | Average of 6 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 184.54 | K | N/A | Wilhoit, Chao, et al., 1985 | Uncertainty assigned by TRC = 0.02 K; TRC |
Ttriple | 184.51 | K | N/A | Counsell, Hales, et al., 1965 | Uncertainty assigned by TRC = 0.05 K; TRC |
Ttriple | 183.9 | K | N/A | Parks, 1925 | Uncertainty assigned by TRC = 0.2 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 562. ± 2. | K | AVG | N/A | Average of 21 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 45. ± 4. | bar | AVG | N/A | Average of 10 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 | 3.65 ± 0.06 | mol/l | AVG | N/A | Average of 7 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 52. ± 3. | kJ/mol | AVG | N/A | Average of 15 out of 16 values; Individual data points |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
43.29 | 390.9 | N/A | Majer and Svoboda, 1985 | |
46.0 | 372. | EB | Muñoz and Krähenbühl, 2001 | Based on data from 357. to 389. K.; AC |
38.2 | 423. | N/A | Wormald and Fennell, 2000 | AC |
29.6 | 473. | N/A | Wormald and Fennell, 2000 | AC |
20.8 | 523. | N/A | Wormald and Fennell, 2000 | AC |
49.9 | 330. | N/A | Dejoz, Cruz Burguet, et al., 1995 | Based on data from 315. to 390. K.; AC |
45.3 | 379. | N/A | Susial and Ortega, 1993 | Based on data from 364. to 403. K.; AC |
45.3 | 387. | A | Stephenson and Malanowski, 1987 | Based on data from 376. to 399. K.; AC |
50.1 | 338. | A | Stephenson and Malanowski, 1987 | Based on data from 323. to 413. K.; AC |
41.9 | 428. | A | Stephenson and Malanowski, 1987 | Based on data from 413. to 550. K.; AC |
51.6 | 236. | A | Stephenson and Malanowski, 1987 | Based on data from 209. to 251. K.; AC |
45.4 | 386. | A | Stephenson and Malanowski, 1987 | Based on data from 376. to 397. K.; AC |
43.8 | 406. | A | Stephenson and Malanowski, 1987 | Based on data from 391. to 429. K.; AC |
41.9 | 430. | A | Stephenson and Malanowski, 1987 | Based on data from 415. to 501. K.; AC |
37.4 | 512. | A | Stephenson and Malanowski, 1987 | Based on data from 497. to 563. K.; AC |
47.2 | 366. | EB | Stephenson and Malanowski, 1987 | Based on data from 351. to 397. K. See also Ambrose, Counsell, et al., 1970.; AC |
49.0 | 344. | N/A | Sachek, Peshchenko, et al., 1982 | Based on data from 329. to 391. K.; AC |
49.5 ± 0.1 | 333. | C | Svoboda, Veselý, et al., 1973 | AC |
48.6 ± 0.1 | 343. | C | Svoboda, Veselý, et al., 1973 | AC |
47.5 ± 0.1 | 353. | C | Svoboda, Veselý, et al., 1973 | AC |
46.4 ± 0.1 | 363. | C | Svoboda, Veselý, et al., 1973 | AC |
55.0 | 303. | N/A | Wilhoit and Zwolinski, 1973 | Based on data from 288. to 404. K.; AC |
53.0 | 310. | DTA | Kemme and Kreps, 1969 | Based on data from 295. to 391. K.; AC |
47.2 ± 0.1 | 356. | C | Counsell, Hales, et al., 1965 | AC |
45.4 ± 0.1 | 381. | C | Counsell, Hales, et al., 1965 | AC |
43.1 ± 0.1 | 391. | C | Counsell, Hales, et al., 1965 | AC |
42.1 | 434. | N/A | Ambrose and Townsend, 1963 | Based on data from 419. to 563. K.; AC |
46.6 | 377. | EB | Biddiscombe, Collerson, et al., 1963 | Based on data from 362. to 398. K.; AC |
48.3 | 352. | N/A | Brown and Smith, 1959 | Based on data from 337. to 390. K. See also Boublik, Fried, et al., 1984.; AC |
48.3 | 352. | N/A | Kahlbaum, 1898 | Based on data from 314. to 390. K. See also Boublik, Fried, et al., 1984.; 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 410. |
---|---|
A (kJ/mol) | 62.53 |
α | -0.6584 |
β | 0.696 |
Tc (K) | 562.9 |
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 |
---|---|---|---|---|---|
295.8 to 391.0 | 4.54607 | 1351.555 | -93.34 | Kemme and Kreps, 1969 | |
391. to 479. | 4.39031 | 1254.502 | -105.246 | Hessel and Geiseler, 1965 | Coefficents calculated by NIST from author's data. |
419.34 to 562.98 | 4.42921 | 1305.001 | -94.676 | Ambrose and Townsend, 1963, 2 | Coefficents calculated by NIST from author's data. |
362.36 to 398.84 | 4.50393 | 1313.878 | -98.789 | Biddiscombe, Collerson, et al., 1963, 2 | Coefficents calculated by NIST from author's data. |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
9.372 | 184.5 | Counsell, Hales, et al., 1965, 2 | DH |
9.28 | 183.9 | Acree, 1991 | AC |
9.280 | 183.9 | Parks, 1925, 2 | DH |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
50.79 | 184.5 | Counsell, Hales, et al., 1965, 2 | DH |
50.46 | 183.9 | Parks, 1925, 2 | DH |
Henry's Law data
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: 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 |
---|---|---|---|---|
130. | 7200. | M | N/A | |
120. | C | N/A | ||
53. | M | N/A | Value at T = 303. K. | |
110. | M | Buttery, Ling, et al., 1969 | ||
140. | M | N/A | ||
120. | M | Butler, Ramchandani, et al., 1935 | This paper supersedes earlier work with more concentrated solutions Butler, Thomson, et al., 1933. |
References
Go To: Top, Gas phase thermochemistry data, Phase change data, Henry's Law data, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
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]
Chermin H.A.G., 1961
Chermin H.A.G.,
Thermo data for petrochemicals. Part 28. Gaseous normal alcohols. The important thermo properties are presented for all the gaseous normal alcohols from methanol through n-decanol,
Petrol. Refiner, 1961, 40 (4), 127-130. [all data]
Buckley E., 1967
Buckley E.,
Chemical equilibria. Part 2. Dehydrogenation of propanol and butanol,
Trans. Faraday Soc., 1967, 63, 895-901. [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]
Dyatkina M.E., 1954
Dyatkina M.E.,
Thermodynamic functions of normal alcohols (propanol, butanol, ethylene glycol),
Zh. Fiz. Khim., 1954, 28, 377. [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]
Counsell, Hales, et al., 1965
Counsell, J.F.; Hales, J.L.; Martin, J.F.,
Thermodynamic properties of organic oxygen compounds. Part 16.?Butyl alcohol,
Trans. Faraday Soc., 1965, 61, 1869, https://doi.org/10.1039/tf9656101869
. [all data]
Parks, 1925
Parks, G.S.,
Thermal data on organic compounds: I the heat capacities and free energies of methyl, ethyl and n-butyl alcohol,
J. Am. Chem. Soc., 1925, 47, 338-45. [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]
Muñoz and Krähenbühl, 2001
Muñoz, Laura A.L.; Krähenbühl, M. Alvina,
Isobaric Vapor Liquid Equilibrium (VLE) Data of the Systems n -Butanol + Butyric Acid and n -Butanol + Acetic Acid,
J. Chem. Eng. Data, 2001, 46, 1, 120-124, https://doi.org/10.1021/je000033u
. [all data]
Wormald and Fennell, 2000
Wormald, C.J.; Fennell, D.P.,
Organometallics, 2000, 21, 3, 767-779, https://doi.org/10.1023/A:1006648903706
. [all data]
Dejoz, Cruz Burguet, et al., 1995
Dejoz, Ana; Cruz Burguet, M.; Munoz, Rosa; Sanchotello, Margarita,
Isobaric Vapor-Liquid Equilibria of Tetrachloroethylene with 1-Butanol and 2-Butanol at 6 and 20 kPa,
J. Chem. Eng. Data, 1995, 40, 1, 290-292, https://doi.org/10.1021/je00017a064
. [all data]
Susial and Ortega, 1993
Susial, Pedro; Ortega, Juan,
Isobaric vapor-liquid equilibria in the system methyl propanoate + n-butyl alcohol,
J. Chem. Eng. Data, 1993, 38, 4, 647-649, https://doi.org/10.1021/je00012a044
. [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]
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]
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]
Kemme and Kreps, 1969
Kemme, Herbert R.; Kreps, Saul I.,
Vapor pressure of primary n-alkyl chlorides and alcohols,
J. Chem. Eng. Data, 1969, 14, 1, 98-102, https://doi.org/10.1021/je60040a011
. [all data]
Ambrose and Townsend, 1963
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]
Brown and Smith, 1959
Brown, I.; Smith, F.,
Liquid-Vapour Equilibria. IX. The Systems n-Propanol + Benzene and n-Butanol + Benzene at 45°C,
Aust. J. Chem., 1959, 12, 3, 407-621, https://doi.org/10.1071/CH9590407
. [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]
Kahlbaum, 1898
Kahlbaum, G.W.A.,
Z. Phys. Chem., Stoechiom. Verwandtschaftsl., 1898, 26, 577. [all data]
Hessel and Geiseler, 1965
Hessel, D.; Geiseler, G.,
Uber die Druckabhangigkeit des heteroazeotropen Systems n-Butanol/Wasser,
Z. Phys. Chem. (Leipzig), 1965, 229, 199-209. [all data]
Ambrose and Townsend, 1963, 2
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, Hales, et al., 1965, 2
Counsell, J.F.; Hales, J.L.; Martin, J.F.,
Thermodynamic properties of organic oxygen compounds. Part 16. Butyl alcohol,
Trans. Faraday Soc., 1965, 61, 1869-1875. [all data]
Acree, 1991
Acree, William E.,
Thermodynamic properties of organic compounds: enthalpy of fusion and melting point temperature compilation,
Thermochimica Acta, 1991, 189, 1, 37-56, https://doi.org/10.1016/0040-6031(91)87098-H
. [all data]
Parks, 1925, 2
Parks, G.S.,
Thermal data on organic compounds I. The heat capacities and free energies of methyl, ethyl and normal-butyl alcohols,
J. Am. Chem. Soc., 1925, 47, 338-345. [all data]
Buttery, Ling, et al., 1969
Buttery, R.G.; Ling, L.C.; Guadagni, D.G.,
Volatilities Aldehydes, Ketones, and Esters in Dilute Water Solution,
J. Agric. Food Chem., 1969, 17, 385-389. [all data]
Butler, Ramchandani, et al., 1935
Butler, J.A.V.; Ramchandani, C.N.; Thomson, D.W.,
The Solubility of Non-Electrolytes. Part 1. The Free Energy of Hydration of Some Alphatic Alcohols,
J. Chem. Soc., 1935, 280-285, https://doi.org/10.1039/jr9350000280
. [all data]
Butler, Thomson, et al., 1933
Butler, J.A.V.; Thomson, D.W.; Maclennan, W.H.,
The Free Energy of the Normal Aliphatic Alcohols in Aqueous Solution. Part I. The Partial Vapor Pressures of Aqueous Solutions of Methyl, n-Propyl, and n-Butyl Alcohols. Part II. THe Solubilities of,
J. Chem. Soc., 1933, 1933, 674-686. [all data]
Notes
Go To: Top, Gas phase thermochemistry data, Phase change data, Henry's Law data, References
- Symbols used in this document:
Cp,gas Constant pressure heat capacity of gas Pc Critical pressure S°gas Entropy of gas at standard conditions 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 ΔfH°gas Enthalpy of formation of gas at standard conditions 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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