Pentane
- Formula: C5H12
- Molecular weight: 72.1488
- IUPAC Standard InChIKey: OFBQJSOFQDEBGM-UHFFFAOYSA-N
- CAS Registry Number: 109-66-0
- 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. - Other names: n-Pentane; Skellysolve A; n-C5H12; Pentan; Pentanen; Pentani; Amyl hydride; NSC 72415
- 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:
BS - Robert L. Brown and Stephen E. Stein
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, Chris Muzny director
AC - William E. Acree, Jr., James S. Chickos
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 |
---|---|---|---|---|---|
Tboil | 309.2 ± 0.2 | K | AVG | N/A | Average of 81 out of 94 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 143.4 ± 0.7 | K | AVG | N/A | Average of 30 out of 31 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 143.46 ± 0.05 | K | AVG | N/A | Average of 6 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 469.8 ± 0.5 | K | AVG | N/A | Average of 27 out of 31 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 33.6 ± 0.6 | bar | AVG | N/A | Average of 20 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Vc | 0.311 | l/mol | N/A | Ambrose and Tsonopoulos, 1995 | |
Vc | 0.3098 | l/mol | N/A | Aftienjew and Zawisza, 1977 | Uncertainty assigned by TRC = 0.0003 l/mol; TRC |
Vc | 0.295 | l/mol | N/A | Beattie, Levine, et al., 1951 | Uncertainty assigned by TRC = 0.006 l/mol; TRC |
Vc | 0.31482 | l/mol | N/A | Sage and Lacey, 1942 | Uncertainty assigned by TRC = 0.0031 l/mol; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 3.22 ± 0.07 | mol/l | AVG | N/A | Average of 14 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 26.5 ± 0.6 | kJ/mol | AVG | N/A | Average of 11 values; Individual data points |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
25.79 | 309.2 | N/A | Majer and Svoboda, 1985 | |
26.200 | 298.15 | N/A | Messerly and Kennedy, 1940 | P = 68.68 kPa; DH |
26.7 | 323. | N/A | Pfohl, Riebesell, et al., 2002 | Based on data from 308. to 423. K.; AC |
29.8 | 238. | A | Stephenson and Malanowski, 1987 | Based on data from 223. to 352. K.; AC |
32.3 | 208. | A | Stephenson and Malanowski, 1987 | Based on data from 143. to 223. K.; AC |
26.1 | 365. | A | Stephenson and Malanowski, 1987 | Based on data from 350. to 422. K.; AC |
26.2 | 433. | A | Stephenson and Malanowski, 1987 | Based on data from 418. to 470. K.; AC |
27.9 | 284. | EB | Stephenson and Malanowski, 1987 | Based on data from 269. to 341. K. See also Osborn and Douslin, 1974.; AC |
25.5 | 310. | N/A | Das, Reed, et al., 1977 | AC |
23. | 350. | N/A | Das, Reed, et al., 1977 | AC |
19.7 | 390. | N/A | Das, Reed, et al., 1977 | AC |
15.1 | 430. | N/A | Das, Reed, et al., 1977 | AC |
8.5 | 460. | N/A | Das, Reed, et al., 1977 | 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) | 260. to 428. |
---|---|
A (kJ/mol) | 37.01 |
α | -0.1238 |
β | 0.4121 |
Tc (K) | 469.6 |
Reference | Majer and Svoboda, 1985 |
Entropy of vaporization
ΔvapS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
87.88 | 298.15 | Messerly and Kennedy, 1940 | P; DH |
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 |
---|---|---|---|---|---|
268.8 to 341.37 | 3.9892 | 1070.617 | -40.454 | Osborn and Douslin, 1974 | Coefficents calculated by NIST from author's data. |
Enthalpy of sublimation
ΔsubH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
42.0 | 143. | B | Bondi, 1963 | AC |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
8.401 | 143.47 | Messerly, Guthrie, et al., 1967 | DH |
8.4149 | 143.46 | Messerly and Kennedy, 1940 | DH |
8.4 | 143.5 | Acree, 1991 | AC |
8.376 | 143.4 | Parks and Huffman, 1930 | DH |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
58.56 | 143.47 | Messerly, Guthrie, et al., 1967 | DH |
58.66 | 143.46 | Messerly and Kennedy, 1940 | DH |
58.41 | 143.4 | Parks and Huffman, 1930 | 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.
Ambrose and Tsonopoulos, 1995
Ambrose, D.; Tsonopoulos, C.,
Vapor-Liquid Critical Properties of Elements and Compounds. 2. Normal Alkenes,
J. Chem. Eng. Data, 1995, 40, 531-546. [all data]
Aftienjew and Zawisza, 1977
Aftienjew, J.; Zawisza, A.,
High-Pressure Liquid Vapour-Equilibria, Critical State and p(V,T,x) Up to 501.15 K and 4.560 MPa for n-Pentane + n-Perfluoropentane,
J. Chem. Thermodyn., 1977, 9, 2, 153-165, https://doi.org/10.1016/0021-9614(77)90081-7
. [all data]
Beattie, Levine, et al., 1951
Beattie, J.A.; Levine, S.W.; Douslin, D.R.,
The vapor pressure and critical constants of normal pentane,
J. Am. Chem. Soc., 1951, 73, 4431. [all data]
Sage and Lacey, 1942
Sage, B.H.; Lacey, W.N.,
Phase equilibria in hydrocarbon systems. Thermodynamic properties of n- pentane.,
Ind. Eng. Chem., 1942, 34, 730-737. [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]
Messerly and Kennedy, 1940
Messerly, G.H.; Kennedy, R.M.,
The heat capacity and entropy, heats of fusion and vaporization and the vapor pressure of n-pentane,
J. Am. Chem. Soc., 1940, 62, 2988-2991. [all data]
Pfohl, Riebesell, et al., 2002
Pfohl, Oliver; Riebesell, Christine; Dohrn, Ralf,
Measurement and calculation of phase equilibria in the system n-pentane + poly(dimethylsiloxane) at 308.15--423.15 K,
Fluid Phase Equilibria, 2002, 202, 2, 289-306, https://doi.org/10.1016/S0378-3812(02)00123-1
. [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]
Osborn and Douslin, 1974
Osborn, Ann G.; Douslin, Donald R.,
Vapor-pressure relations for 15 hydrocarbons,
J. Chem. Eng. Data, 1974, 19, 2, 114-117, https://doi.org/10.1021/je60061a022
. [all data]
Das, Reed, et al., 1977
Das, Tarun R.; Reed, Charles O.; Eubank, Philip T.,
PVT surface and thermodynamic properties of n-pentane,
J. Chem. Eng. Data, 1977, 22, 1, 3-9, https://doi.org/10.1021/je60072a014
. [all data]
Bondi, 1963
Bondi, A.,
Heat of Siblimation of Molecular Crystals: A Catalog of Molecular Structure Increments.,
J. Chem. Eng. Data, 1963, 8, 3, 371-381, https://doi.org/10.1021/je60018a027
. [all data]
Messerly, Guthrie, et al., 1967
Messerly, J.F.; Guthrie, G.B.; Todd, S.S.; Finke, H.L.,
Low-temperature thermal data for n-pentane, n-heptadecane, and n-octadecane,
J. Chem. Eng. Data, 1967, 12, 338-346. [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 and Huffman, 1930
Parks, G.S.; Huffman, H.M.,
Thermal data on organic compounds. IX. A study of the effect of unsaturation on the heat capacities, entropies and free energies of some hydrocarbons and other compounds,
J. Am. Chem. Soc., 1930, 52, 4381-4391. [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 ΔsubH Enthalpy of sublimation ΔvapH Enthalpy of vaporization ΔvapH° Enthalpy of vaporization at standard conditions ΔvapS Entropy of vaporization 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.