1-Propanol
- Formula: C3H8O
- Molecular weight: 60.0950
- IUPAC Standard InChIKey: BDERNNFJNOPAEC-UHFFFAOYSA-N
- CAS Registry Number: 71-23-8
- 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: Propyl alcohol; n-Propan-1-ol; n-Propanol; n-Propyl alcohol; Ethylcarbinol; Optal; Osmosol extra; Propanol; Propylic alcohol; 1-Propyl alcohol; n-C3H7OH; 1-Hydroxypropane; Propanol-1; Propan-1-ol; n-Propyl alkohol; Alcool propilico; Alcool propylique; Propanole; Propanolen; Propanoli; Propylowy alkohol; UN 1274; Propylan-propyl alcohol; NSC 30300; Alcohol, propyl
- Permanent link for this species. Use this link for bookmarking this species for future reference.
- Information on this page:
- Other data available:
- Data at other public NIST sites:
- Options:
Data at NIST subscription sites:
- NIST / TRC Web Thermo Tables, "lite" edition (thermophysical and thermochemical data)
- NIST / TRC Web Thermo Tables, professional edition (thermophysical and thermochemical data)
NIST subscription sites provide data under the NIST Standard Reference Data Program, but require an annual fee to access. The purpose of the fee is to recover costs associated with the development of data collections included in such sites. Your institution may already be a subscriber. Follow the links above to find out more about the data in these sites and their terms of usage.
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 | 370.3 ± 0.5 | K | AVG | N/A | Average of 127 out of 139 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 146.7 | K | N/A | Tschamler, Richter, et al., 1949 | Uncertainty assigned by TRC = 0.5 K; TRC |
Tfus | 147. | K | N/A | Timmermans, 1935 | Uncertainty assigned by TRC = 3. K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 148.75 | K | N/A | Wilhoit, Chao, et al., 1985 | Uncertainty assigned by TRC = 0.02 K; TRC |
Ttriple | 148.75 | K | N/A | Counsell, Lees, et al., 1968 | Uncertainty assigned by TRC = 0.02 K; TRC |
Ttriple | 147.0 | K | N/A | Parks and Huffman, 1926 | Uncertainty assigned by TRC = 0.3 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 536.9 ± 0.8 | K | AVG | N/A | Average of 20 out of 25 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 52. ± 1. | bar | AVG | N/A | Average of 12 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Vc | 0.218 | l/mol | N/A | Gude and Teja, 1995 | |
Vc | 0.216 | l/mol | N/A | Zawisza and Vejrosta, 1982 | Uncertainty assigned by TRC = 0.001 l/mol; Visual; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 4.58 ± 0.06 | mol/l | AVG | N/A | Average of 7 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 47. ± 1. | kJ/mol | AVG | N/A | Average of 15 values; Individual data points |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
41.44 | 370.3 | N/A | Majer and Svoboda, 1985 | |
41.2 | 371. | N/A | Wormald and Vine, 2000 | AC |
35.2 | 423. | N/A | Wormald and Vine, 2000 | AC |
29.4 | 453. | N/A | Wormald and Vine, 2000 | AC |
21.0 | 498. | N/A | Wormald and Vine, 2000 | AC |
11.4 | 528. | N/A | Wormald and Vine, 2000 | AC |
47.0 | 318. | N/A | Aucejo, Gonzalez-Alfaro, et al., 1995 | Based on data from 303. to 370. K.; AC |
42.9 | 375. | N/A | Ortega, Susial, et al., 1990 | Based on data from 360. to 377. K.; AC |
48.0 | 214. | A | Stephenson and Malanowski, 1987 | Based on data from 200. to 228. K.; AC |
43.5 | 366. | A | Stephenson and Malanowski, 1987 | Based on data from 356. to 376. K.; AC |
42.3 | 384. | A | Stephenson and Malanowski, 1987 | Based on data from 369. to 407. K.; AC |
40.1 | 416. | A | Stephenson and Malanowski, 1987 | Based on data from 401. to 482. K.; AC |
36.5 | 492. | A | Stephenson and Malanowski, 1987 | Based on data from 478. to 507. K.; AC |
46.4 ± 0.1 | 313. | C | Svoboda, Veselý, et al., 1973 | AC |
45.7 ± 0.1 | 323. | C | Svoboda, Veselý, et al., 1973 | AC |
44.9 ± 0.1 | 333. | C | Svoboda, Veselý, et al., 1973 | AC |
44.0 ± 0.1 | 343. | C | Svoboda, Veselý, et al., 1973 | AC |
43.2 ± 0.1 | 353. | C | Svoboda, Veselý, et al., 1973 | AC |
42.4 ± 0.1 | 363. | C | Svoboda, Veselý, et al., 1973 | AC |
49.3 | 290. | N/A | Wilhoit and Zwolinski, 1973 | Based on data from 275. to 373. K.; AC |
44.7 | 348. | EB | Ambrose, Counsell, et al., 1970 | Based on data from 333. to 377. K. See also Stephenson and Malanowski, 1987.; AC |
46.9 | 307. | DTA | Kemme and Kreps, 1969 | Based on data from 292. to 370. K.; AC |
46.7 | 303. | N/A | Van Ness, Soczek, et al., 1967 | Based on data from 288. to 348. K.; AC |
40.7 | 420. | N/A | Ambrose and Townsend, 1963 | Based on data from 405. to 537. K.; AC |
44.3 | 353. | EB | Biddiscombe, Collerson, et al., 1963 | Based on data from 338. to 378. K.; AC |
44.1 | 358. | N/A | Mathews and McKetta, 1961 | Based on data from 343. to 385. K.; AC |
43.9 ± 0.1 | 343. | C | Mathews and McKetta, 1961 | AC |
42.3 ± 0.1 | 360. | C | Mathews and McKetta, 1961 | AC |
41.2 ± 0.1 | 370. | C | Mathews and McKetta, 1961 | AC |
40.3 ± 0.1 | 378. | C | Mathews and McKetta, 1961 | AC |
39.7 ± 0.1 | 384. | C | Mathews and McKetta, 1961 | AC |
45.5 | 321. to 367. | N/A | Aronovich, Kastorskii, et al., 1959 | AC |
43.2 | 354. | N/A | Williamson and Harrison, 1957 | AC |
44.99 ± 0.42 | 333.13 | V | Williamson and Harrison, 1957, 2 | 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 390. |
---|---|
A (kJ/mol) | 52.06 |
α | -0.8386 |
β | 0.6888 |
Tc (K) | 536.7 |
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 |
---|---|---|---|---|---|
333.32 to 377.72 | 4.87601 | 1441.629 | -74.299 | Ambrose and Sprake, 1970 | Coefficents calculated by NIST from author's data. |
292.4 to 370.5 | 5.31384 | 1690.864 | -51.804 | Kemme and Kreps, 1969 | |
405.46 to 536.71 | 4.59871 | 1300.491 | -86.364 | Ambrose and Townsend, 1963, 2 | Coefficents calculated by NIST from author's data. |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
5.372 | 148.75 | Counsell, Lees, et al., 1968, 2 | DH |
5.4 | 148.7 | van Miltenburg and van den Berg, 2004 | AC |
5.37 | 148.8 | Counsell, Lees, et al., 1968 | AC |
5.192 | 147.0 | Parks and Huffman, 1926, 2 | DH |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
36.11 | 148.75 | Counsell, Lees, et al., 1968, 2 | DH |
35.3 | 147.0 | Parks and Huffman, 1926, 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.
Tschamler, Richter, et al., 1949
Tschamler, H.; Richter, E.; Wettig, F.,
Mixtures of Primry Aliphatic Alcohols with Chlorex and Other Organic Substances. Binary Liquid Mixtures XII.,
Monatsh. Chem., 1949, 80, 749. [all data]
Timmermans, 1935
Timmermans, J.,
Researches in Stoichiometry. I. The Heat of Fusion of Organic Compounds.,
Bull. Soc. Chim. Belg., 1935, 44, 17-40. [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]
Parks and Huffman, 1926
Parks, G.S.; Huffman, H.M.,
Thermal data on organic compounds: IV the heat capacites, entropies, and free energies of normal propyl alcohol, ethyl ether, and dulcitol,
J. Am. Chem. Soc., 1926, 48, 2788-93. [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]
Zawisza and Vejrosta, 1982
Zawisza, A.; Vejrosta, J.,
High-pressure liquid-vapor equilibria, critical stat, and p(V, T, x) up to 573.15 K and 5.066 MPa for (heptane + propan-1-ol),
J. Chem. Thermodyn., 1982, 14, 239-49. [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]
Wormald and Vine, 2000
Wormald, C.J.; Vine, M.D.,
Specific enthalpy increments for propan-1-ol at temperatures up to 573.2 K and 11.3 MPa,
The Journal of Chemical Thermodynamics, 2000, 32, 3, 329-339, https://doi.org/10.1006/jcht.1999.0594
. [all data]
Aucejo, Gonzalez-Alfaro, et al., 1995
Aucejo, Antonio; Gonzalez-Alfaro, Vicenta; Monton, Juan B.; Vazquez, M. Isabel,
Isobaric Vapor-Liquid Equilibria of Trichloroethylene with 1-Propanol and 2-Propanol at 20 and 100 kPa,
J. Chem. Eng. Data, 1995, 40, 1, 332-335, https://doi.org/10.1021/je00017a073
. [all data]
Ortega, Susial, et al., 1990
Ortega, Juan; Susial, Pedro; De Alfonso, Casiano,
Isobaric vapor-liquid equilibrium of methyl butanoate with ethanol and 1-propanol binary systems,
J. Chem. Eng. Data, 1990, 35, 2, 216-219, https://doi.org/10.1021/je00060a037
. [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]
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]
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]
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]
Van Ness, Soczek, et al., 1967
Van Ness, Hendrick C.; Soczek, C.A.; Peloquin, G.L.; Machado, R.L.,
Thermodynamic excess properties of three alcohol-hydrocarbon systems,
J. Chem. Eng. Data, 1967, 12, 2, 217-224, https://doi.org/10.1021/je60033a017
. [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]
Mathews and McKetta, 1961
Mathews, J.F.; McKetta, J.J.,
THE THERMODYNAMIC PROPERTIES OF n-PROPYL ALCOHOL,
J. Phys. Chem., 1961, 65, 5, 758-762, https://doi.org/10.1021/j100823a013
. [all data]
Aronovich, Kastorskii, et al., 1959
Aronovich, Kh.A.; Kastorskii, L.P.; Fedorova, K.F.,
Zh. Fiz. Khim., 1959, 41, 20. [all data]
Williamson and Harrison, 1957
Williamson, Kenneth D.; Harrison, Roland H.,
Heats of Vaporization of 1,1,2-Trichloroethane, 1-Propanol, and 2-Propanol; Vapor Heat Capacity of 1,1,2-Trichloroethane,
J. Chem. Phys., 1957, 26, 6, 1409, https://doi.org/10.1063/1.1743555
. [all data]
Williamson and Harrison, 1957, 2
Williamson, K.D.; Harrison, R.H.,
Heats of vaporization of 1,1,2-trichloroethane, 1-propanol, and 2-propanol; vapor heat capacity of 1,1,2-trichloroethane,
J. Chem. Phys., 1957, 26, 1409-14. [all data]
Ambrose and Sprake, 1970
Ambrose, D.; Sprake, C.H.S.,
Thermodynamic properties of organic oxygen compounds XXV. Vapour pressures and normal boiling temperatures of aliphatic alcohols,
The Journal of Chemical Thermodynamics, 1970, 2, 5, 631-645, https://doi.org/10.1016/0021-9614(70)90038-8
. [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]
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]
van Miltenburg and van den Berg, 2004
van Miltenburg, J. Cees; van den Berg, Gerrit J.K.,
Heat Capacities and Derived Thermodynamic Functions of 1-Propanol between 10 K and 350 K and of 1-Pentanol between 85 K and 370 K,
J. Chem. Eng. Data, 2004, 49, 3, 735-739, https://doi.org/10.1021/je0499768
. [all data]
Parks and Huffman, 1926, 2
Parks, G.S.; Huffman, H.M.,
Thermal data on organic compounds. IV. The heat capacities, entropies and free energies of normal propyl alcohol, ethyl ether and dulcitol,
J. Am. Chem. Soc., 1926, 48, 2788-2793. [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
- The National Institute of Standards and Technology (NIST) uses its best efforts to deliver a high quality copy of the Database and to verify that the data contained therein have been selected on the basis of sound scientific judgment. However, NIST makes no warranties to that effect, and NIST shall not be liable for any damage that may result from errors or omissions in the Database.
- Customer support for NIST Standard Reference Data products.