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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Condensed phase thermochemistry data
Go To: Top, 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 as indicated in comments:
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
DH - Eugene S. Domalski and Elizabeth D. Hearing
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔfH°liquid | -328. ± 4. | kJ/mol | AVG | N/A | Average of 7 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -2670. ± 20. | kJ/mol | AVG | N/A | Average of 10 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
S°liquid | 225.73 | J/mol*K | N/A | Counsell, Hales, et al., 1965 | DH |
S°liquid | 228.0 | J/mol*K | N/A | Parks, Kelley, et al., 1929 | Extrapolation below 90 K, 46.02 J/mol*K. Revision of previous data.; DH |
S°liquid | 251.9 | J/mol*K | N/A | Parks, 1925 | Extrapolation below 90 K, 73.81 J/mol*K.; DH |
Constant pressure heat capacity of liquid
Cp,liquid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
176.86 | 298.15 | Andreoli-Ball, Patterson, et al., 1988 | DH |
176.67 | 298.15 | Gates, Wood, et al., 1986 | T = 298.15 to 368.15 K.; DH |
177.7 | 298. | Korolev, Kukharenko, et al., 1986 | DH |
192.2 | 321.05 | Naziev, Bashirov, et al., 1986 | T = 321.05, 349.20, 373.35 K. p = 0.1 MPa. Unsmoothed experimental datum given as 2.5934 kJ/kg*K.; DH |
177.18 | 298.15 | Ogawa and Murakami, 1986 | DH |
175.97 | 298.15 | Roux-Dexgranges, Grolier, et al., 1986 | DH |
176.69 | 298.15 | Tanaka, Toyama, et al., 1986 | DH |
177.08 | 298.15 | Zegers and Somsen, 1984 | DH |
174.3 | 293.15 | Arutyunyan, Bagdasaryan, et al., 1981 | T = 293 to 373 K. p = 0.1 MPa. Unsmoothed experimental datum given as 2.351 kJ/kg*K. Cp given from 293.15 to 533.15 for pressure range 10 to 60 MPa.; DH |
181.6 | 303.5 | Griigo'ev, Yanin, et al., 1979 | T = 303 to 462 K. p = 0.98 bar.; DH |
179.5 | 301.2 | Paz Andrade, Paz, et al., 1970 | T = 28, 40°C.; DH |
177.03 | 298.15 | Counsell, Hales, et al., 1965 | T = 11 to 323 K.; DH |
189.1 | 323. | Swietoslawski and Zielenkiewicz, 1960 | Mean value 21 to 78°C.; DH |
215.5 | 302.6 | Phillip, 1939 | DH |
183.3 | 298. | Trew and Watkins, 1933 | DH |
175.3 | 294.0 | Parks, 1925 | T = 90 to 294 K. Value is unsmoothed experimental datum.; DH |
180.3 | 303. | Willams and Daniels, 1924 | T = 303 to 343 K. Equation only.; DH |
174.5 | 298. | von Reis, 1881 | T = 290 to 390 K.; DH |
Phase change data
Go To: Top, Condensed phase thermochemistry 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, 2 | Uncertainty assigned by TRC = 0.05 K; TRC |
Ttriple | 183.9 | K | N/A | Parks, 1925, 2 | 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, 2 | AC |
45.4 ± 0.1 | 381. | C | Counsell, Hales, et al., 1965, 2 | AC |
43.1 ± 0.1 | 391. | C | Counsell, Hales, et al., 1965, 2 | 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)
View plot Requires a JavaScript / HTML 5 canvas capable browser.
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 | DH |
9.28 | 183.9 | Acree, 1991 | AC |
9.280 | 183.9 | Parks, 1925 | DH |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
50.79 | 184.5 | Counsell, Hales, et al., 1965 | DH |
50.46 | 183.9 | Parks, 1925 | DH |
References
Go To: Top, Condensed phase thermochemistry data, Phase change data, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
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, 1869-1875. [all data]
Parks, Kelley, et al., 1929
Parks, G.S.; Kelley, K.K.; Huffman, H.M.,
Thermal data on organic compounds. V. A revision of the entropies and free energies of nineteen organic compounds,
J. Am. Chem. Soc., 1929, 51, 1969-1973. [all data]
Parks, 1925
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]
Andreoli-Ball, Patterson, et al., 1988
Andreoli-Ball, L.; Patterson, D.; Costas, M.; Caceres-Alonso, M.,
Heat capacity and corresponding states in alkan-1-ol-n-alkane systems, J. Chem. Soc.,
Faraday Trans. 1, 1988, 84(11), 3991-4012. [all data]
Gates, Wood, et al., 1986
Gates, J.A.; Wood, R.H.; Cobos, J.C.; Casanova, C.; Roux, A.H.; Roux-Desgranges, G.; Grolier, J.-P.E.,
Densities and heat capacities of 1-butanol + n-decane from 298 K to 400 K,
Fluid Phase Equilib., 1986, 27, 137-151. [all data]
Korolev, Kukharenko, et al., 1986
Korolev, V.P.; Kukharenko, V.A.; Krestov, G.A.,
Specific heat of binary mixtures of aliphatic alcohols with N,N-dimethylformamide and dimethylsulphoxide,
Zhur. Fiz. Khim., 1986, 60, 1854-1857. [all data]
Naziev, Bashirov, et al., 1986
Naziev, Ya.M.; Bashirov, M.M.; Badalov, Yu.A.,
Experimental device for measurement of isobaric specific heat of electrolytes at elevated pressures,
Inzh-Fiz. Zhur., 1986, 51(5), 789-795. [all data]
Ogawa and Murakami, 1986
Ogawa, H.; Murakami, S.,
Excess isobaric heat capacities for water + alkanol mixtures at 298.15 K,
Thermochim. Acta, 1986, 109, 145-154. [all data]
Roux-Dexgranges, Grolier, et al., 1986
Roux-Dexgranges, G.; Grolier, J.-P.E.; Villamanan, M.A.; Casanova, C.,
Role of alcohol in microemulsions. III. Volumes and heat capacities in the continuious phase water-n-butanol-toluene of reverse micelles,
Fluid Phase Equilibria, 1986, 25, 209-230. [all data]
Tanaka, Toyama, et al., 1986
Tanaka, R.; Toyama, S.; Murakami, S.,
Heat capacities of {xCnH2n+1OH+(1-x)C7H16} for n = 1 to 6 at 298.15 K,
J. Chem. Thermodynam., 1986, 18, 63-73. [all data]
Zegers and Somsen, 1984
Zegers, H.C.; Somsen, G.,
Partial molar volumes and heat capacities in (dimethylformamide + an n-alkanol),
J. Chem. Thermodynam., 1984, 16, 225-235. [all data]
Arutyunyan, Bagdasaryan, et al., 1981
Arutyunyan, G.S.; Bagdasaryan, S.S.; Kerimov, A.M.,
Experimental investigation of the isobaric heat capacity of n-propyl, n-butyl and n-amyl alcohols at different temperatures and pressures,
Izv. Akad. Nauk Azerb. SSr, 1981, (6), 94-97. [all data]
Griigo'ev, Yanin, et al., 1979
Griigo'ev, B.A.; Yanin, G.S.; Rastorguev, Yu.L.; Thermophysical parameters of alcohols, Tr. GIAP,
54, 1979, 57-64. [all data]
Paz Andrade, Paz, et al., 1970
Paz Andrade, M.I.; Paz, J.M.; Recacho, E.,
Contribucion a la microcalorimetria de los calores especificos de solidos y liquidos,
An. Quim., 1970, 66, 961-967. [all data]
Swietoslawski and Zielenkiewicz, 1960
Swietoslawski, W.; Zielenkiewicz, A.,
Mean specific heat in homologous series of binary and ternary positive azeotropes,
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Phillip, 1939
Phillip, N.M.,
Adiabatic and isothermal compressibilities of liquids,
Proc. Indian Acad. Sci., 1939, A9, 109-120. [all data]
Trew and Watkins, 1933
Trew, V.C.G.; Watkins, G.M.C.,
Some physical properties of mixtures of certain organic liquids,
Trans. Faraday Soc., 1933, 29, 1310-1318. [all data]
Willams and Daniels, 1924
Willams, J.W.; Daniels, F.,
The specific heats of certain organic liquids at elevated temperatures,
J. Am. Chem. Soc., 1924, 46, 903-917. [all data]
von Reis, 1881
von Reis, M.A.,
Die specifische Wärme flüssiger organischer Verbindungen und ihre Beziehung zu deren Moleculargewicht,
Ann. Physik [3], 1881, 13, 447-464. [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, 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, https://doi.org/10.1039/tf9656101869
. [all data]
Parks, 1925, 2
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
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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,
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Susial and Ortega, 1993
Susial, Pedro; Ortega, Juan,
Isobaric vapor-liquid equilibria in the system methyl propanoate + n-butyl alcohol,
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. [all data]
Stephenson and Malanowski, 1987
Stephenson, Richard M.; Malanowski, Stanislaw,
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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,
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. [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,
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Wilhoit and Zwolinski, 1973
Wilhoit, R.C.; Zwolinski, B.J.,
Physical and thermodynamic properties of aliphatic alcohols,
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Kemme and Kreps, 1969
Kemme, Herbert R.; Kreps, Saul I.,
Vapor pressure of primary n-alkyl chlorides and alcohols,
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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,
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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.,
364. Thermodynamic properties of organic oxygen compounds. Part VIII. Purification and vapour pressures of the propyl and butyl alcohols,
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Brown and Smith, 1959
Brown, I.; Smith, F.,
Liquid-Vapour Equilibria. IX. The Systems n-Propanol + Benzene and n-Butanol + Benzene at 45°C,
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. [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,
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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,
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. [all data]
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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,
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. [all data]
Acree, 1991
Acree, William E.,
Thermodynamic properties of organic compounds: enthalpy of fusion and melting point temperature compilation,
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. [all data]
Notes
Go To: Top, Condensed phase thermochemistry data, Phase change data, References
- Symbols used in this document:
Cp,liquid Constant pressure heat capacity of liquid Pc Critical pressure S°liquid Entropy of liquid at standard conditions Tboil Boiling point Tc Critical temperature Tfus Fusion (melting) point Ttriple Triple point temperature Vc Critical volume ΔcH°liquid Enthalpy of combustion of liquid at standard conditions ΔfH°liquid Enthalpy of formation of liquid 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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