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
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Condensed phase thermochemistry data
Go To: Top, Phase change data, Reaction thermochemistry 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 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 | -41.47 ± 0.14 | kcal/mol | Ccb | Good, 1970 | ALS |
ΔfH°liquid | -41.36 ± 0.16 | kcal/mol | Ccb | Prosen and Rossini, 1945 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -838.68 ± 0.11 | kcal/mol | Ccb | Good, 1970 | Corresponding ΔfHºliquid = -41.47 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -838.80 ± 0.14 | kcal/mol | Ccb | Prosen and Rossini, 1945 | Corresponding ΔfHºliquid = -41.35 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -838.71 ± 0.18 | kcal/mol | Ccb | Prosen and Rossini, 1944 | Corresponding ΔfHºliquid = -41.44 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS |
Quantity | Value | Units | Method | Reference | Comment |
S°liquid | 62.971 | cal/mol*K | N/A | Messerly, Guthrie, et al., 1967 | DH |
S°liquid | 62.780 | cal/mol*K | N/A | Messerly and Kennedy, 1940 | DH |
S°liquid | 62.00 | cal/mol*K | N/A | Parks and Huffman, 1930 | Extrapolation below 90 K, 56.61 J/mol*K.; DH |
Constant pressure heat capacity of liquid
Cp,liquid (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
40.30 | 298. | Grigor'ev, Rastorguev, et al., 1975 | T = 300 to 463 K.; DH |
39.959 | 298.15 | Messerly, Guthrie, et al., 1967 | T = 12 to 300 K.; DH |
40.151 | 290. | Messerly and Kennedy, 1940 | T = 12 to 290 K.; DH |
39.01 | 290.0 | Parks and Huffman, 1930 | T = 93 to 290 K. Value is unsmoothed experimental datum.; DH |
Phase change data
Go To: Top, Condensed phase thermochemistry data, Reaction thermochemistry 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 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 | 33.1 ± 0.6 | atm | 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° | 6.3 ± 0.2 | kcal/mol | AVG | N/A | Average of 11 values; Individual data points |
Enthalpy of vaporization
ΔvapH (kcal/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
6.164 | 309.2 | N/A | Majer and Svoboda, 1985 | |
6.2620 | 298.15 | N/A | Messerly and Kennedy, 1940 | P = 68.68 kPa; DH |
6.38 | 323. | N/A | Pfohl, Riebesell, et al., 2002 | Based on data from 308. to 423. K.; AC |
7.12 | 238. | A | Stephenson and Malanowski, 1987 | Based on data from 223. to 352. K.; AC |
7.72 | 208. | A | Stephenson and Malanowski, 1987 | Based on data from 143. to 223. K.; AC |
6.24 | 365. | A | Stephenson and Malanowski, 1987 | Based on data from 350. to 422. K.; AC |
6.26 | 433. | A | Stephenson and Malanowski, 1987 | Based on data from 418. to 470. K.; AC |
6.67 | 284. | EB | Stephenson and Malanowski, 1987 | Based on data from 269. to 341. K. See also Osborn and Douslin, 1974.; AC |
6.09 | 310. | N/A | Das, Reed, et al., 1977 | AC |
5.5 | 350. | N/A | Das, Reed, et al., 1977 | AC |
4.71 | 390. | N/A | Das, Reed, et al., 1977 | AC |
3.61 | 430. | N/A | Das, Reed, et al., 1977 | AC |
2.0 | 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)
(kcal/mol)
Tr = reduced temperature (T / Tc)
View plot Requires a JavaScript / HTML 5 canvas capable browser.
Temperature (K) | 260. to 428. |
---|---|
A (kcal/mol) | 8.846 |
α | -0.1238 |
β | 0.4121 |
Tc (K) | 469.6 |
Reference | Majer and Svoboda, 1985 |
Entropy of vaporization
ΔvapS (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
21.00 | 298.15 | Messerly and Kennedy, 1940 | P; DH |
Antoine Equation Parameters
log10(P) = A − (B / (T + C))
P = vapor pressure (atm)
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 | 3.9835 | 1070.617 | -40.454 | Osborn and Douslin, 1974 | Coefficents calculated by NIST from author's data. |
Enthalpy of sublimation
ΔsubH (kcal/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
10.0 | 143. | B | Bondi, 1963 | AC |
Enthalpy of fusion
ΔfusH (kcal/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
2.008 | 143.47 | Messerly, Guthrie, et al., 1967 | DH |
2.0112 | 143.46 | Messerly and Kennedy, 1940 | DH |
2.0 | 143.5 | Acree, 1991 | AC |
2.002 | 143.4 | Parks and Huffman, 1930 | DH |
Entropy of fusion
ΔfusS (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
14.00 | 143.47 | Messerly, Guthrie, et al., 1967 | DH |
14.02 | 143.46 | Messerly and Kennedy, 1940 | DH |
13.96 | 143.4 | Parks and Huffman, 1930 | DH |
Reaction thermochemistry data
Go To: Top, Condensed 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 as indicated in comments:
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
MS - José A. Martinho Simões
Note: Please consider using the reaction search for this species. This page allows searching of all reactions involving this species. A general reaction search form is also available. Future versions of this site may rely on reaction search pages in place of the enumerated reaction displays seen below.
Individual Reactions
By formula: C5H10 + H2 = C5H12
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -30.27 ± 0.58 | kcal/mol | Chyd | Molnar, Rachford, et al., 1984 | liquid phase; solvent: Dioxane; ALS |
ΔrH° | -29.87 ± 0.42 | kcal/mol | Chyd | Molnar, Rachford, et al., 1984 | liquid phase; solvent: Hexane; ALS |
ΔrH° | -29.30 ± 0.57 | kcal/mol | Chyd | Rogers and Skanupong, 1974 | liquid phase; solvent: Hexane; ALS |
ΔrH° | -28.5 ± 0.3 | kcal/mol | Chyd | Rogers and McLafferty, 1971 | liquid phase; solvent: Hydrocarbon; ALS |
C10H12CrO5 (solution) = (solution) + C5CrO5 (solution)
By formula: C10H12CrO5 (solution) = C5H12 (solution) + C5CrO5 (solution)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 8.91 | kcal/mol | N/A | Morse, Parker, et al., 1989 | solvent: Pentane; The reaction enthalpy was derived by using the LPHP value for the enthalpy of cleavage of Cr-CO bond in Cr(CO)6, 36.81 kcal/mol Lewis, Golden, et al., 1984, toghether with a PAC value for the reaction Cr(CO)6(solution) + n-C5H12(solution) = Cr(CO)5(n-C5H12)(solution) + CO(solution), 27.89 kcal/mol Morse, Parker, et al., 1989; MS |
(solution) + (solution) = C10H12CrO5 (solution) + (solution)
By formula: C5H12 (solution) + C6CrO6 (solution) = C10H12CrO5 (solution) + CO (solution)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 27.9 ± 2.5 | kcal/mol | PAC | Morse, Parker, et al., 1989 | solvent: Pentane; The reaction enthalpy relies on 0.67 for the quantum yield of CO dissociation; MS |
By formula: 3H2 + C5H6 = C5H12
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -96.8 ± 0.1 | kcal/mol | Chyd | Roth, Adamczak, et al., 1991 | liquid phase; ALS |
ΔrH° | -95.6 ± 1.1 | kcal/mol | Chyd | Skinner and Snelson, 1959 | liquid phase; solvent: Acetic acid; ALS |
By formula: 3H2 + C5H6 = C5H12
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -97.0 ± 0.3 | kcal/mol | Chyd | Roth, Adamczak, et al., 1991 | liquid phase; ALS |
ΔrH° | -96.0 ± 0.4 | kcal/mol | Chyd | Skinner and Snelson, 1959 | liquid phase; solvent: Acetic acid; ALS |
By formula: 2H2 + C5H8 = C5H12
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -60.22 ± 0.15 | kcal/mol | Chyd | Kistiakowsky, Ruhoff, et al., 1936 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -60.79 ± 0.15 kcal/mol; At 355 °K; ALS |
(solution) + C5H11BrMg (solution) = C6H5BrMgO (solution) + (solution)
By formula: C6H6O (solution) + C5H11BrMg (solution) = C6H5BrMgO (solution) + C5H12 (solution)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -48.4 ± 1.0 | kcal/mol | RSC | Holm, 1983 | solvent: Diethyl ether; MS |
C5H11BrMg (solution) + (g) = (solution) + Br2Mg (solution)
By formula: C5H11BrMg (solution) + HBr (g) = C5H12 (solution) + Br2Mg (solution)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -73.21 ± 0.53 | kcal/mol | RSC | Holm, 1981 | solvent: Diethyl ether; MS |
(solution) + C5H11BrMg (solution) = C2H5BrMgO (solution) + (solution)
By formula: C2H6O (solution) + C5H11BrMg (solution) = C2H5BrMgO (solution) + C5H12 (solution)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -47.7 ± 1.0 | kcal/mol | RSC | Holm, 1983 | solvent: Diethyl ether; MS |
C5H11BrMg (solution) + (solution) = CH4BrMgN (solution) + (solution)
By formula: C5H11BrMg (solution) + CH5N (solution) = CH4BrMgN (solution) + C5H12 (solution)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -31.19 ± 0.60 | kcal/mol | RSC | Holm, 1983 | solvent: Diethyl ether; MS |
By formula: 2H2 + C5H8 = C5H12
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -65.5 ± 0.2 | kcal/mol | Chyd | Roth, Kirmse, et al., 1982 | liquid phase; solvent: Isooctane; ALS |
C5O5W (g) + (g) = C10H12O5W (g)
By formula: C5O5W (g) + C5H12 (g) = C10H12O5W (g)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -10.6 ± 3.0 | kcal/mol | EqG | Brown, Ishikawa, et al., 1990 | Temperature range: ca. 300-350 K; MS |
C5H11BrMg (solution) + (solution) = (solution) + CH3BrMg (solution)
By formula: C5H11BrMg (solution) + CH4 (solution) = C5H12 (solution) + CH3BrMg (solution)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -3.6 ± 1.0 | kcal/mol | RSC | Holm, 1983 | solvent: Diethyl ether; MS |
(solution) + C5H11BrMg (solution) = C3HBrMgN2 (solution) + (solution)
By formula: C3H2N2 (solution) + C5H11BrMg (solution) = C3HBrMgN2 (solution) + C5H12 (solution)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -48.59 | kcal/mol | RSC | Holm, 1983 | solvent: Diethyl ether; MS |
(solution) + C5H11BrMg (solution) = C12H10BrMgN (solution) + (solution)
By formula: C12H11N (solution) + C5H11BrMg (solution) = C12H10BrMgN (solution) + C5H12 (solution)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -28.39 | kcal/mol | RSC | Holm, 1983 | solvent: Diethyl ether; MS |
C5H11BrMg (solution) + (solution) = C2BrF3MgO2 (solution) + (solution)
By formula: C5H11BrMg (solution) + C2HF3O2 (solution) = C2BrF3MgO2 (solution) + C5H12 (solution)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -65.39 | kcal/mol | RSC | Holm, 1983 | solvent: Diethyl ether; MS |
C5H11BrMg (solution) + (solution) = C6BrF5MgO (cr) + (solution)
By formula: C5H11BrMg (solution) + C6HF5O (solution) = C6BrF5MgO (cr) + C5H12 (solution)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -55.90 | kcal/mol | RSC | Holm, 1983 | solvent: Diethyl ether; MS |
C5H11BrMg (solution) + (solution) = C2H2BrF3MgO (solution) + (solution)
By formula: C5H11BrMg (solution) + C2H3F3O (solution) = C2H2BrF3MgO (solution) + C5H12 (solution)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -47.71 | kcal/mol | RSC | Holm, 1983 | solvent: Diethyl ether; MS |
(solution) + C5H11BrMg (solution) = CH3BrMgO (cr) + (solution)
By formula: CH4O (solution) + C5H11BrMg (solution) = CH3BrMgO (cr) + C5H12 (solution)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -52.51 | kcal/mol | RSC | Holm, 1983 | solvent: Diethyl ether; MS |
By formula: 2H2 + C5H8 = C5H12
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -54.11 ± 0.15 | kcal/mol | Chyd | Dolliver, Gresham, et al., 1937 | gas phase; At 355 °K; ALS |
By formula: C5H12 = C5H12
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -1.861 | kcal/mol | Eqk | Pines, Kvetinskas, et al., 1945 | gas phase; Heat of isomerization; ALS |
By formula: H2 + C5H10 = C5H12
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -28.1 ± 0.2 | kcal/mol | Chyd | Egger and Benson, 1966 | gas phase; ALS |
By formula: H2 + C5H10 = C5H12
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -27.2 ± 0.2 | kcal/mol | Chyd | Egger and Benson, 1966 | gas phase; ALS |
Gas phase ion energetics data
Go To: Top, Condensed phase thermochemistry data, Phase change data, Reaction 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 evaluated as indicated in comments:
L - Sharon G. Lias
Data compiled as indicated in comments:
LL - Sharon G. Lias and Joel F. Liebman
LBLHLM - Sharon G. Lias, John E. Bartmess, Joel F. Liebman, John L. Holmes, Rhoda D. Levin, and W. Gary Mallard
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) | 10.28 ± 0.10 | eV | N/A | N/A | L |
Ionization energy determinations
IE (eV) | Method | Reference | Comment |
---|---|---|---|
10.37 | PI | Traeger, Hudson, et al., 1996 | T = 0K; LL |
10.43 | EST | Luo and Pacey, 1992 | LL |
10.22 ± 0.05 | EI | Holmes and Lossing, 1991 | LL |
10.28 ± 0.10 | EVAL | Lias, 1982 | LBLHLM |
10.18 ± 0.15 | EQ | Mautner(Meot-Ner), Sieck, et al., 1981 | LLK |
10.93 | PE | Kimura, Katsumata, et al., 1981 | LLK |
10.2 ± 0.1 | PE | Bieri, Burger, et al., 1977 | LLK |
10.50 | EQ | Lias, Ausloos, et al., 1976 | LLK |
10.36 | PE | Ikuta, Yoshihara, et al., 1973 | LLK |
10.59 ± 0.05 | EI | Flesch and Svec, 1973 | LLK |
10.37 | PE | Dewar and Worley, 1969 | RDSH |
10.35 | PI | Watanabe, Nakayama, et al., 1962 | RDSH |
10.9 ± 0.1 | PE | Bieri, Burger, et al., 1977 | Vertical value; LLK |
Appearance energy determinations
Ion | AE (eV) | Other Products | Method | Reference | Comment |
---|---|---|---|---|---|
C3H6+ | 11.02 | C2H6 | PI | Traeger, Hudson, et al., 1996 | T = 0K; LL |
C3H6+ | 10.99 ± 0.02 | C2H6 | PI | Steiner, Giese, et al., 1961 | RDSH |
C3H7+ | 11.13 | C2H5 | PI | Traeger, Hudson, et al., 1996 | T = 0K; LL |
C3H7+ | 11.11 ± 0.05 | C2H5 | PI | Steiner, Giese, et al., 1961 | RDSH |
C4H8+ | 11.05 | CH4 | PI | Traeger, Hudson, et al., 1996 | T = 0K; LL |
C4H8+ | 11.00 | CH4 | EI | Wolkoff and Holmes, 1978 | LLK |
C4H8+ | 10.93 ± 0.03 | CH4 | PI | Steiner, Giese, et al., 1961 | RDSH |
C4H9+ | 11.10 | CH3 | PI | Traeger, Hudson, et al., 1996 | T = 0K; LL |
C4H9+ | 11.0 ± 0.1 | CH3 | EI | Burgers and Holmes, 1982 | LBLHLM |
C4H9+ | 10.98 ± 0.05 | CH3 | EI | Lossing and Semeluk, 1970 | RDSH |
C4H9+ | 11.06 ± 0.07 | CH3 | PI | Steiner, Giese, et al., 1961 | RDSH |
References
Go To: Top, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Gas phase ion energetics data, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Good, 1970
Good, W.D.,
The enthalpies of combustion and formation of the isomeric pentanes,
J. Chem. Thermodyn., 1970, 2, 237-244. [all data]
Prosen and Rossini, 1945
Prosen, E.J.; Rossini, F.D.,
Heats of combustion and formation of the paraffin hydrocarbons at 25° C,
J. Res. NBS, 1945, 263-267. [all data]
Prosen and Rossini, 1944
Prosen, E.J.; Rossini, F.D.,
Heats of combustion of eight normal paraffin hydrocarbons in the liquid state,
J. Res. NBS, 1944, 33, 255-272. [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]
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]
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]
Grigor'ev, Rastorguev, et al., 1975
Grigor'ev, B.A.; Rastorguev, Yu.L.; Yanin, G.S.,
Experimental determination of the isobaric specific heat of n-alkanes,
Iz. Vyssh. Uchebn. Zaved. Neft Gaz 18, 1975, No.10, 63-66. [all data]
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]
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.,
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Notes
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- Symbols used in this document:
AE Appearance energy Cp,liquid Constant pressure heat capacity of liquid IE (evaluated) Recommended ionization energy 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 ΔrH° Enthalpy of reaction at standard conditions 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
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