n-Hexane
- Formula: C6H14
- Molecular weight: 86.1754
- IUPAC Standard InChIKey: VLKZOEOYAKHREP-UHFFFAOYSA-N
- CAS Registry Number: 110-54-3
- 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. - Isotopologues:
- Other names: Hexane; Skellysolve B; n-C6H14; Esani; Heksan; Hexanen; Hexyl hydride; Gettysolve-B; NCI-C60571; NSC 68472
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Gas phase thermochemistry 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 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 | -39.94 | kcal/mol | N/A | Good and Smith, 1969 | Value computed using ΔfHliquid° value of -198.7±0.7 kj/mol from Good and Smith, 1969 and ΔvapH° value of 31.6 kj/mol from Prosen and Rossini, 1945.; DRB |
ΔfH°gas | -39.96 ± 0.19 | kcal/mol | Ccb | Prosen and Rossini, 1945 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
S°gas | 92.93 ± 0.20 | cal/mol*K | N/A | Scott D.W., 1974 | This reference does not contain the original experimental data. Experimental entropy value is based on the results [ Messerly J.F., 1967] for S(liquid).; GT |
Constant pressure heat capacity of gas
Cp,gas (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
26.429 | 200. | Scott D.W., 1974, 2 | Recommended values were obtained from the consistent correlation scheme for alkanes [ Scott D.W., 1974, Scott D.W., 1974, 2]. This approach gives a better agreement with experimental data than the statistical thermodynamics calculation [ Pitzer K.S., 1944, Pitzer K.S., 1946] (see also [ Waddington G., 1949]).; GT |
31.919 | 273.15 | ||
34.08 ± 0.05 | 298.15 | ||
34.240 | 300. | ||
43.389 | 400. | ||
51.931 | 500. | ||
59.300 | 600. | ||
65.500 | 700. | ||
70.801 | 800. | ||
75.301 | 900. | ||
79.199 | 1000. | ||
82.500 | 1100. | ||
85.399 | 1200. | ||
88.000 | 1300. | ||
90.000 | 1400. | ||
93.000 | 1500. |
Constant pressure heat capacity of gas
Cp,gas (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
37.349 ± 0.074 | 333.85 | Waddington G., 1947 | GT |
40.220 ± 0.081 | 365.15 | ||
43.301 ± 0.086 | 398.85 | ||
46.391 ± 0.093 | 433.70 | ||
49.460 ± 0.098 | 468.90 |
Condensed phase thermochemistry data
Go To: Top, Gas 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 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 | -47.48 ± 0.16 | kcal/mol | Ccb | Good and Smith, 1969 | ALS |
ΔfH°liquid | -47.52 ± 0.19 | kcal/mol | Ccb | Prosen and Rossini, 1945 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -995. ± 4. | kcal/mol | AVG | N/A | Average of 6 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
S°liquid | 70.760 | cal/mol*K | N/A | Douslin and Huffman, 1946 | DH |
S°liquid | 69.19 | cal/mol*K | N/A | Stull, 1937 | Extrapolation below 91 K, 54.68 J/mol*K.; DH |
S°liquid | 70.60 | cal/mol*K | N/A | Huffman, Parks, et al., 1931 | Extrapolation below 90 K, 64.02 J/mol*K.; DH |
S°liquid | 71.10 | cal/mol*K | N/A | Parks, Huffman, et al., 1930 | Extrapolation below 90 K, 65.44 J/mol*K.; DH |
Constant pressure heat capacity of liquid
Cp,liquid (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
63.38 | 298.15 | Pruzan, 1991 | DH |
46.730 | 298.15 | Ohnishi, Fujihara, et al., 1989 | DH |
47.242 | 298.15 | Andreoli-Ball, Patterson, et al., 1988 | DH |
47.242 | 298.15 | Perez-Casas, Aicart, et al., 1988 | DH |
46.759 | 298.15 | Saito and Tanaka, 1988 | DH |
46.807 | 298.15 | Benson and D'Arcy, 1986 | DH |
48.52 | 308.35 | Naziev, Bashirov, et al., 1986 | T = 308.35, 333.15. p = 0.1 MPa. Unsmoothed experimental datum given as 2.356 kJ/kg*K.; DH |
47.242 | 298.15 | Tardajos, Aicart, et al., 1986 | DH |
46.597 | 298.15 | Costas and Patterson, 1985 | T = 283.15, 298.15, 313.15 K.; DH |
46.797 | 298.15 | Benson, D'Arcy, et al., 1984 | DH |
46.685 | 298.15 | Bravo, Pintos, et al., 1984 | DH |
46.87 | 297.32 | Grigor'ev and Andolenko, 1984 | T = 293 to 324 K. Unsmoothed experimental datum given as 2.276 kJ/kg*K.; DH |
46.797 | 298.15 | Aicart, Kumaran, et al., 1983 | DH |
46.797 | 298.15 | Benson, D'Arcy, et al., 1983 | DH |
46.685 | 298.15 | Wilhelm, Inglese, et al., 1982 | DH |
46.63 | 298. | Zaripov, 1982 | T = 298, 323 K.; DH |
46.788 | 298.15 | Grolier, Inglese, et al., 1981 | DH |
46.759 | 297.316 | Kalinowska, Jedlinska, et al., 1980 | T = 185 to 300 K. Unsmoothed experimental datum.; DH |
44.02 | 300. | Czarnota, 1979 | DH |
46.89 | 298. | Grigor'ev, Rastorguev, et al., 1975 | T = 300 to 463 K.; DH |
47.44 | 298.15 | Diaz pena and Renuncio, 1974 | T = 298 to 325 K.; DH |
46.869 | 299.8 | Connolly, Sage, et al., 1951 | T = 80 to 200°F.; DH |
46.599 | 298.15 | Douslin and Huffman, 1946 | T = 13 to 300 K.; DH |
44.50 | 300.7 | Phillip, 1939 | DH |
45.20 | 298.1 | Stull, 1937 | T = 90 to 320 K. Hump about 262 K with abnormal curve to 320 K.; DH |
46.20 | 293.5 | Huffman, Parks, et al., 1931 | T = 140 to 294 K. Value is unsmoothed experimental datum.; DH |
45.79 | 295.1 | Parks, Huffman, et al., 1930 | T = 90 to 295 K. Value is unsmoothed experimental datum.; DH |
46.39 | 298. | von Reis, 1881 | T = 290 to 363 K.; DH |
Phase change data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry 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 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
DH - Eugene S. Domalski and Elizabeth D. Hearing
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 341.9 ± 0.3 | K | AVG | N/A | Average of 85 out of 100 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 178. ± 1. | K | AVG | N/A | Average of 32 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 178.0 ± 0.5 | K | AVG | N/A | Average of 9 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 507.6 ± 0.5 | K | AVG | N/A | Average of 39 out of 44 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 29.8 ± 0.4 | atm | AVG | N/A | Average of 24 out of 25 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Vc | 0.368 | l/mol | N/A | Ambrose and Tsonopoulos, 1995 | |
Vc | 0.371 | l/mol | N/A | Zawisza, 1985 | Uncertainty assigned by TRC = 0.007 l/mol; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 2.71 ± 0.02 | mol/l | AVG | N/A | Average of 10 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 7.5 ± 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 |
---|---|---|---|---|
6.895 | 341.9 | N/A | Majer and Svoboda, 1985 | |
8.34 | 253. | A | Stephenson and Malanowski, 1987 | Based on data from 238. to 298. K.; AC |
8.53 | 244. | A | Stephenson and Malanowski, 1987 | Based on data from 189. to 259. K.; AC |
7.53 | 313. | A | Stephenson and Malanowski, 1987 | Based on data from 298. to 343. K.; AC |
7.19 | 356. | A | Stephenson and Malanowski, 1987 | Based on data from 341. to 377. K.; AC |
7.00 | 389. | A | Stephenson and Malanowski, 1987 | Based on data from 374. to 451. K.; AC |
7.03 | 460. | A | Stephenson and Malanowski, 1987 | Based on data from 445. to 508. K.; AC |
7.65 | 301. | A,MM | Stephenson and Malanowski, 1987 | Based on data from 286. to 343. K. See also Willingham, Taylor, et al., 1945.; AC |
6.36 | 373. | C | Wormald and Yerlett, 1985 | AC |
5.38 | 423. | C | Wormald and Yerlett, 1985 | AC |
3.75 | 473. | C | Wormald and Yerlett, 1985 | AC |
2.1 | 498. | C | Wormald and Yerlett, 1985 | AC |
7.39 | 313. | N/A | Michou-Saucet, Jose, et al., 1984 | Based on data from 298. to 338. K.; AC |
7.34 ± 0.02 | 313. | C | Majer, Svoboda, et al., 1979 | AC |
7.05 ± 0.02 | 333. | C | Majer, Svoboda, et al., 1979 | AC |
6.74 ± 0.02 | 353. | C | Majer, Svoboda, et al., 1979 | AC |
7.55 | 310. | N/A | Letcher and Marsicano, 1974 | Based on data from 300. to 321. K. See also Boublik, Fried, et al., 1984.; AC |
7.77 | 250. | N/A | Carruth and Kobayashi, 1973 | Based on data from 178. to 265. K.; AC |
7.39 ± 0.02 | 309. | C | Waddington and Douslin, 1947 | AC |
7.12 ± 0.02 | 328. | C | Waddington and Douslin, 1947 | AC |
7.29 ± 0.05 | 313. | C | Lemons and Felsing, 1943 | AC |
6.93 ± 0.05 | 333. | C | Lemons and Felsing, 1943 | AC |
6.74 ± 0.05 | 353. | C | Lemons and Felsing, 1943 | 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) | 298. to 444. |
---|---|
A (kcal/mol) | 10.48 |
α | -0.039 |
β | 0.397 |
Tc (K) | 507.4 |
Reference | Majer and Svoboda, 1985 |
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 |
---|---|---|---|---|---|
177.70 to 264.93 | 3.45033 | 1044.038 | -53.893 | Carruth and Kobayashi, 1973 | Coefficents calculated by NIST from author's data. |
286.18 to 342.69 | 3.99695 | 1171.53 | -48.784 | Williamham, Taylor, et al., 1945 |
Enthalpy of sublimation
ΔsubH (kcal/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
12.1 | 178. | B | Bondi, 1963 | AC |
Enthalpy of fusion
ΔfusH (kcal/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
3.1260 | 177.84 | Douslin and Huffman, 1946 | DH |
3.126 | 177.8 | Domalski and Hearing, 1996 | AC |
2.9500 | 177.90 | Stull, 1937 | DH |
3.1150 | 177.9 | Huffman, Parks, et al., 1931 | DH |
3.0069 | 178.6 | Parks, Huffman, et al., 1930 | DH |
Entropy of fusion
ΔfusS (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
17.58 | 177.84 | Douslin and Huffman, 1946 | DH |
16.58 | 177.90 | Stull, 1937 | DH |
17.5 | 177.9 | Huffman, Parks, et al., 1931 | DH |
16.84 | 178.6 | Parks, Huffman, et al., 1930 | DH |
Reaction thermochemistry data
Go To: Top, Gas phase thermochemistry data, Condensed 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 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: H2 + C6H12 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -30.0 ± 0.6 | kcal/mol | AVG | N/A | Average of 8 values; Individual data points |
By formula: 2H2 + C6H10 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -60.3 ± 0.4 | kcal/mol | Chyd | Fang and Rogers, 1992 | liquid phase; solvent: Cyclohexane; ALS |
ΔrH° | -60.69 ± 0.65 | kcal/mol | Chyd | Molnar, Rachford, et al., 1984 | liquid phase; solvent: Dioxane; ALS |
ΔrH° | -60.17 ± 0.37 | kcal/mol | Chyd | Turner, Mallon, et al., 1973 | liquid phase; solvent: Glacial acetic acid; ALS |
ΔrH° | -60.03 ± 0.10 | kcal/mol | Chyd | Kistiakowsky, Ruhoff, et al., 1936 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -60.53 ± 0.15 kcal/mol; At 355 °K; ALS |
By formula: H2 + C6H12 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -27.75 ± 0.11 | kcal/mol | Chyd | Rogers, Crooks, et al., 1987 | liquid phase; ALS |
ΔrH° | -115.0 ± 0.83 | kcal/mol | Chyd | Rogers and Crooks, 1983 | liquid phase; solvent: Hexane; ALS |
ΔrH° | -26.59 ± 0.27 | kcal/mol | Chyd | Rogers, Papadimetriou, et al., 1975 | liquid phase; solvent: Hexane; ALS |
By formula: H2 + C6H12 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -29.06 ± 0.076 | kcal/mol | Chyd | Rogers, Crooks, et al., 1987 | liquid phase; ALS |
ΔrH° | -28.52 ± 0.29 | kcal/mol | Chyd | Rogers, Papadimetriou, et al., 1975 | liquid phase; solvent: Hexane; ALS |
ΔrH° | -28.57 ± 0.29 | kcal/mol | Chyd | Rogers and Siddiqui, 1975 | liquid phase; solvent: n-Hexane; ALS |
By formula: C6H12 + H2 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -28.18 ± 0.17 | kcal/mol | Chyd | Rogers, Crooks, et al., 1987 | liquid phase; ALS |
ΔrH° | -28.18 ± 0.20 | kcal/mol | Chyd | Rogers and Crooks, 1983 | liquid phase; solvent: Hexane; ALS |
ΔrH° | -26.24 ± 0.41 | kcal/mol | Chyd | Rogers, Papadimetriou, et al., 1975 | liquid phase; solvent: Hexane; ALS |
By formula: H2 + C6H12 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -28.56 ± 0.16 | kcal/mol | Chyd | Rogers, Crooks, et al., 1987 | liquid phase; ALS |
ΔrH° | -28.44 ± 0.19 | kcal/mol | Chyd | Rogers and Crooks, 1983 | liquid phase; solvent: Hexane; ALS |
ΔrH° | -27.05 ± 0.22 | kcal/mol | Chyd | Rogers, Papadimetriou, et al., 1975 | liquid phase; solvent: Hexane; ALS |
By formula: 3H2 + C6H8 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -81.0 ± 0.6 | kcal/mol | Chyd | Fang and Rogers, 1992 | liquid phase; solvent: Cyclohexane; ALS |
ΔrH° | -80.50 ± 0.33 | kcal/mol | Chyd | Turner, Mallon, et al., 1973 | liquid phase; solvent: Glacial acetic acid; ALS |
By formula: 3H2 + C6H8 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -80.0 ± 0.6 | kcal/mol | Chyd | Fang and Rogers, 1992 | liquid phase; solvent: Cyclohexane; ALS |
ΔrH° | -79.43 ± 0.22 | kcal/mol | Chyd | Turner, Mallon, et al., 1973 | liquid phase; solvent: Glacial acetic acid; ALS |
By formula: 4H2 + C6H6 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -139.3 ± 1.0 | kcal/mol | Chyd | Skinner and Snelson, 1959 | liquid phase; solvent: Acetic acid; Reanalyzed by Cox and Pilcher, 1970, Original value = -139.4 ± 1.0 kcal/mol; ALS |
By formula: 2H2 + C6H10 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -53.9 ± 0.3 | kcal/mol | Chyd | Fang and Rogers, 1992 | liquid phase; solvent: Cyclohexane; ALS |
By formula: 2H2 + C6H10 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -52.9 ± 0.3 | kcal/mol | Chyd | Fang and Rogers, 1992 | liquid phase; solvent: Cyclohexane; ALS |
By formula: 2H2 + C6H10 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -52.4 ± 0.4 | kcal/mol | Chyd | Fang and Rogers, 1992 | liquid phase; solvent: Cyclohexane; ALS |
By formula: 2H2 + C6H10 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -58.4 ± 0.4 | kcal/mol | Chyd | Fang and Rogers, 1992 | liquid phase; solvent: Cyclohexane; ALS |
By formula: 2H2 + C6H10 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -57.6 ± 0.4 | kcal/mol | Chyd | Fang and Rogers, 1992 | liquid phase; solvent: Cyclohexane; ALS |
By formula: 2H2 + C6H10 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -51.4 ± 0.4 | kcal/mol | Chyd | Fang and Rogers, 1992 | liquid phase; solvent: Cyclohexane; ALS |
By formula: 2H2 + C6H10 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -50.5 ± 0.4 | kcal/mol | Chyd | Fang and Rogers, 1992 | liquid phase; solvent: Cyclohexane; ALS |
By formula: 2H2 + C6H10 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -63.0 ± 0.2 | kcal/mol | Chyd | Roth, Kirmse, et al., 1982 | liquid phase; solvent: Isooctane; ALS |
By formula: 4H2 + C6H6 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -124.7 ± 0.4 | kcal/mol | Chyd | Roth, Hopf, et al., 1994 | liquid phase; solvent: Isooctane; ALS |
C5O5W (g) + (g) = C11H14O5W (g)
By formula: C5O5W (g) + C6H14 (g) = C11H14O5W (g)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -10.8 ± 3.0 | kcal/mol | EqG | Brown, Ishikawa, et al., 1990 | Temperature range: ca. 300-350 K; MS |
By formula: 2H2 + C6H10 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -69.16 ± 0.11 | kcal/mol | Chyd | Rogers, Dagdagan, et al., 1979 | liquid phase; solvent: Hexane; ALS |
By formula: 2H2 + C6H10 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -65.11 ± 0.28 | kcal/mol | Chyd | Rogers, Dagdagan, et al., 1979 | liquid phase; solvent: Hexane; ALS |
By formula: 2H2 + C6H10 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -65.7 ± 0.4 | kcal/mol | Chyd | Rogers, Dagdagan, et al., 1979 | liquid phase; solvent: Hexane; ALS |
By formula: C6H14 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -1.30 ± 0.21 | kcal/mol | Ciso | Prosen and Rossini, 1941 | liquid phase; Calculated from ΔHc; ALS |
By formula: C6H14 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -0.76 ± 0.19 | kcal/mol | Ciso | Prosen and Rossini, 1941 | liquid phase; Calculated from ΔHc; ALS |
By formula: C6H14 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -1.96 ± 0.20 | kcal/mol | Ciso | Prosen and Rossini, 1941 | liquid phase; Calculated from ΔHc; ALS |
By formula: C6H14 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -3.49 ± 0.18 | kcal/mol | Ciso | Prosen and Rossini, 1941 | liquid phase; Calculated from ΔHc; ALS |
By formula: 5H2 + C6H4 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -168.5 ± 0.4 | kcal/mol | Chyd | Roth, Adamczak, et al., 1991 | liquid phase; ALS |
By formula: 5H2 + C6H4 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -169.4 ± 0.4 | kcal/mol | Chyd | Roth, Adamczak, et al., 1991 | liquid phase; ALS |
3 + C6H8 =
By formula: 3H2 + C6H8 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -103.2 ± 0.3 | kcal/mol | Chyd | Roth, Adamczak, et al., 1991 | liquid phase; ALS |
References
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Good and Smith, 1969
Good, W.D.; Smith, N.K.,
Enthalpies of combustion of toluene, benzene, cyclohexane, cyclohexene, methylcyclopentane, 1-methylcyclopentene, and n-hexane,
J. Chem. Eng. Data, 1969, 14, 102-106. [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]
Scott D.W., 1974
Scott D.W.,
Correlation of the chemical thermodynamic properties of alkane hydrocarbons,
J. Chem. Phys., 1974, 60, 3144-3165. [all data]
Messerly J.F., 1967
Messerly J.F.,
Low-temperature thermal data for n-pentane, n-heptadecane, and n-octadecane. Revised thermodynamic functions for the n-alkanes, C5-C18,
J. Chem. Eng. Data, 1967, 12, 338-346. [all data]
Scott D.W., 1974, 2
Scott D.W.,
Chemical Thermodynamic Properties of Hydrocarbons and Related Substances. Properties of the Alkane Hydrocarbons, C1 through C10 in the Ideal Gas State from 0 to 1500 K. U.S. Bureau of Mines, Bulletin 666, 1974. [all data]
Pitzer K.S., 1944
Pitzer K.S.,
Thermodynamics of gaseous paraffins. Specific heat and related properties,
Ind. Eng. Chem., 1944, 36, 829-831. [all data]
Pitzer K.S., 1946
Pitzer K.S.,
The entropies and related properties of branched paraffin hydrocarbons,
Chem. Rev., 1946, 39, 435-447. [all data]
Waddington G., 1949
Waddington G.,
Experimental vapor heat capacities and heats of vaporization of 2-methylpentane, 3-methylpentane, and 2,3-dimethylbutane,
J. Am. Chem. Soc., 1949, 71, 3902-3906. [all data]
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Adiabatic and isothermal compressibilities of liquids,
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Carruth, Grant F.; Kobayashi, Riki,
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Molnar, Rachford, et al., 1984
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Kistiakowsky, G.B.; Ruhoff, J.R.; Smith, H.A.; Vaughan, W.E.,
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Enthalpies of hydrogenation of the hexenes,
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Enthalpies of hydrogenation of the isomers of n-hexene,
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An improved hydrogen microcalorimeter for use with large molecules,
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Propargyl-Stabilisierungsenergie,
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Notes
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- Symbols used in this document:
Cp,gas Constant pressure heat capacity of gas Cp,liquid Constant pressure heat capacity of liquid Pc Critical pressure S°gas Entropy of gas at standard conditions 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°gas Enthalpy of formation of gas 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 ρc Critical density - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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