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, Reaction thermochemistry data, Henry's Law 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 | -167.1 | kJ/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 | -167.2 ± 0.79 | kJ/mol | Ccb | Prosen and Rossini, 1945 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
S°gas | 388.82 ± 0.84 | J/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 (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
110.58 | 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 |
133.55 | 273.15 | ||
142.6 ± 0.2 | 298.15 | ||
143.26 | 300. | ||
181.54 | 400. | ||
217.28 | 500. | ||
248.11 | 600. | ||
274.05 | 700. | ||
296.23 | 800. | ||
315.06 | 900. | ||
331.37 | 1000. | ||
345.18 | 1100. | ||
357.31 | 1200. | ||
368.19 | 1300. | ||
376.56 | 1400. | ||
389.11 | 1500. |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
156.27 ± 0.31 | 333.85 | Waddington G., 1947 | GT |
168.28 ± 0.34 | 365.15 | ||
181.17 ± 0.36 | 398.85 | ||
194.10 ± 0.39 | 433.70 | ||
206.94 ± 0.41 | 468.90 |
Condensed phase thermochemistry data
Go To: Top, Gas phase thermochemistry data, Reaction thermochemistry data, Henry's Law 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 | -198.7 ± 0.67 | kJ/mol | Ccb | Good and Smith, 1969 | ALS |
ΔfH°liquid | -198.8 ± 0.79 | kJ/mol | Ccb | Prosen and Rossini, 1945 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -4163. ± 20. | kJ/mol | AVG | N/A | Average of 6 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
S°liquid | 296.06 | J/mol*K | N/A | Douslin and Huffman, 1946 | DH |
S°liquid | 289.5 | J/mol*K | N/A | Stull, 1937 | Extrapolation below 91 K, 54.68 J/mol*K.; DH |
S°liquid | 295.4 | J/mol*K | N/A | Huffman, Parks, et al., 1931 | Extrapolation below 90 K, 64.02 J/mol*K.; DH |
S°liquid | 297.5 | J/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 (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
265.2 | 298.15 | Pruzan, 1991 | DH |
195.52 | 298.15 | Ohnishi, Fujihara, et al., 1989 | DH |
197.66 | 298.15 | Andreoli-Ball, Patterson, et al., 1988 | DH |
197.66 | 298.15 | Perez-Casas, Aicart, et al., 1988 | DH |
195.64 | 298.15 | Saito and Tanaka, 1988 | DH |
195.84 | 298.15 | Benson and D'Arcy, 1986 | DH |
203.0 | 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 |
197.66 | 298.15 | Tardajos, Aicart, et al., 1986 | DH |
194.96 | 298.15 | Costas and Patterson, 1985 | T = 283.15, 298.15, 313.15 K.; DH |
195.80 | 298.15 | Benson, D'Arcy, et al., 1984 | DH |
195.33 | 298.15 | Bravo, Pintos, et al., 1984 | DH |
196.1 | 297.32 | Grigor'ev and Andolenko, 1984 | T = 293 to 324 K. Unsmoothed experimental datum given as 2.276 kJ/kg*K.; DH |
195.80 | 298.15 | Aicart, Kumaran, et al., 1983 | DH |
195.80 | 298.15 | Benson, D'Arcy, et al., 1983 | DH |
195.33 | 298.15 | Wilhelm, Inglese, et al., 1982 | DH |
195.1 | 298. | Zaripov, 1982 | T = 298, 323 K.; DH |
195.76 | 298.15 | Grolier, Inglese, et al., 1981 | DH |
195.64 | 297.316 | Kalinowska, Jedlinska, et al., 1980 | T = 185 to 300 K. Unsmoothed experimental datum.; DH |
184.2 | 300. | Czarnota, 1979 | DH |
196.2 | 298. | Grigor'ev, Rastorguev, et al., 1975 | T = 300 to 463 K.; DH |
198.5 | 298.15 | Diaz pena and Renuncio, 1974 | T = 298 to 325 K.; DH |
196.10 | 299.8 | Connolly, Sage, et al., 1951 | T = 80 to 200°F.; DH |
194.97 | 298.15 | Douslin and Huffman, 1946 | T = 13 to 300 K.; DH |
186.2 | 300.7 | Phillip, 1939 | DH |
189.1 | 298.1 | Stull, 1937 | T = 90 to 320 K. Hump about 262 K with abnormal curve to 320 K.; DH |
193.3 | 293.5 | Huffman, Parks, et al., 1931 | T = 140 to 294 K. Value is unsmoothed experimental datum.; DH |
191.6 | 295.1 | Parks, Huffman, et al., 1930 | T = 90 to 295 K. Value is unsmoothed experimental datum.; DH |
194.1 | 298. | von Reis, 1881 | T = 290 to 363 K.; DH |
Reaction thermochemistry data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Henry's Law 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° | -125. ± 3. | kJ/mol | AVG | N/A | Average of 8 values; Individual data points |
By formula: 2H2 + C6H10 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -252. ± 2. | kJ/mol | Chyd | Fang and Rogers, 1992 | liquid phase; solvent: Cyclohexane; ALS |
ΔrH° | -253.9 ± 2.7 | kJ/mol | Chyd | Molnar, Rachford, et al., 1984 | liquid phase; solvent: Dioxane; ALS |
ΔrH° | -251.8 ± 1.5 | kJ/mol | Chyd | Turner, Mallon, et al., 1973 | liquid phase; solvent: Glacial acetic acid; ALS |
ΔrH° | -251.2 ± 0.42 | kJ/mol | Chyd | Kistiakowsky, Ruhoff, et al., 1936 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -253.3 ± 0.63 kJ/mol; At 355 °K; ALS |
By formula: H2 + C6H12 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -116.1 ± 0.45 | kJ/mol | Chyd | Rogers, Crooks, et al., 1987 | liquid phase; ALS |
ΔrH° | -481.2 ± 3.5 | kJ/mol | Chyd | Rogers and Crooks, 1983 | liquid phase; solvent: Hexane; ALS |
ΔrH° | -111.3 ± 1.1 | kJ/mol | Chyd | Rogers, Papadimetriou, et al., 1975 | liquid phase; solvent: Hexane; ALS |
By formula: H2 + C6H12 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -121.6 ± 0.32 | kJ/mol | Chyd | Rogers, Crooks, et al., 1987 | liquid phase; ALS |
ΔrH° | -119.3 ± 1.2 | kJ/mol | Chyd | Rogers, Papadimetriou, et al., 1975 | liquid phase; solvent: Hexane; ALS |
ΔrH° | -119.5 ± 1.2 | kJ/mol | Chyd | Rogers and Siddiqui, 1975 | liquid phase; solvent: n-Hexane; ALS |
By formula: C6H12 + H2 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -117.9 ± 0.73 | kJ/mol | Chyd | Rogers, Crooks, et al., 1987 | liquid phase; ALS |
ΔrH° | -117.9 ± 0.82 | kJ/mol | Chyd | Rogers and Crooks, 1983 | liquid phase; solvent: Hexane; ALS |
ΔrH° | -109.8 ± 1.7 | kJ/mol | Chyd | Rogers, Papadimetriou, et al., 1975 | liquid phase; solvent: Hexane; ALS |
By formula: H2 + C6H12 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -119.5 ± 0.69 | kJ/mol | Chyd | Rogers, Crooks, et al., 1987 | liquid phase; ALS |
ΔrH° | -119.0 ± 0.78 | kJ/mol | Chyd | Rogers and Crooks, 1983 | liquid phase; solvent: Hexane; ALS |
ΔrH° | -113.2 ± 0.92 | kJ/mol | Chyd | Rogers, Papadimetriou, et al., 1975 | liquid phase; solvent: Hexane; ALS |
By formula: 3H2 + C6H8 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -339. ± 3. | kJ/mol | Chyd | Fang and Rogers, 1992 | liquid phase; solvent: Cyclohexane; ALS |
ΔrH° | -336.8 ± 1.4 | kJ/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° | -335. ± 3. | kJ/mol | Chyd | Fang and Rogers, 1992 | liquid phase; solvent: Cyclohexane; ALS |
ΔrH° | -332.3 ± 0.92 | kJ/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° | -582.8 ± 4.2 | kJ/mol | Chyd | Skinner and Snelson, 1959 | liquid phase; solvent: Acetic acid; Reanalyzed by Cox and Pilcher, 1970, Original value = -583.2 ± 4.2 kJ/mol; ALS |
By formula: 2H2 + C6H10 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -226. ± 1. | kJ/mol | Chyd | Fang and Rogers, 1992 | liquid phase; solvent: Cyclohexane; ALS |
By formula: 2H2 + C6H10 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -221. ± 1. | kJ/mol | Chyd | Fang and Rogers, 1992 | liquid phase; solvent: Cyclohexane; ALS |
By formula: 2H2 + C6H10 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -219. ± 2. | kJ/mol | Chyd | Fang and Rogers, 1992 | liquid phase; solvent: Cyclohexane; ALS |
By formula: 2H2 + C6H10 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -244. ± 2. | kJ/mol | Chyd | Fang and Rogers, 1992 | liquid phase; solvent: Cyclohexane; ALS |
By formula: 2H2 + C6H10 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -241. ± 2. | kJ/mol | Chyd | Fang and Rogers, 1992 | liquid phase; solvent: Cyclohexane; ALS |
By formula: 2H2 + C6H10 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -215. ± 2. | kJ/mol | Chyd | Fang and Rogers, 1992 | liquid phase; solvent: Cyclohexane; ALS |
By formula: 2H2 + C6H10 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -211. ± 2. | kJ/mol | Chyd | Fang and Rogers, 1992 | liquid phase; solvent: Cyclohexane; ALS |
By formula: 2H2 + C6H10 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -264. ± 0.8 | kJ/mol | Chyd | Roth, Kirmse, et al., 1982 | liquid phase; solvent: Isooctane; ALS |
By formula: 4H2 + C6H6 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -522. ± 2. | kJ/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° | -45. ± 13. | kJ/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° | -289.4 ± 0.46 | kJ/mol | Chyd | Rogers, Dagdagan, et al., 1979 | liquid phase; solvent: Hexane; ALS |
By formula: 2H2 + C6H10 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -272.4 ± 1.2 | kJ/mol | Chyd | Rogers, Dagdagan, et al., 1979 | liquid phase; solvent: Hexane; ALS |
By formula: 2H2 + C6H10 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -275. ± 2. | kJ/mol | Chyd | Rogers, Dagdagan, et al., 1979 | liquid phase; solvent: Hexane; ALS |
By formula: C6H14 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -5.44 ± 0.88 | kJ/mol | Ciso | Prosen and Rossini, 1941 | liquid phase; Calculated from ΔHc; ALS |
By formula: C6H14 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -3.2 ± 0.79 | kJ/mol | Ciso | Prosen and Rossini, 1941 | liquid phase; Calculated from ΔHc; ALS |
By formula: C6H14 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -8.20 ± 0.84 | kJ/mol | Ciso | Prosen and Rossini, 1941 | liquid phase; Calculated from ΔHc; ALS |
By formula: C6H14 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -14.6 ± 0.75 | kJ/mol | Ciso | Prosen and Rossini, 1941 | liquid phase; Calculated from ΔHc; ALS |
By formula: 5H2 + C6H4 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -705. ± 2. | kJ/mol | Chyd | Roth, Adamczak, et al., 1991 | liquid phase; ALS |
By formula: 5H2 + C6H4 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -709. ± 2. | kJ/mol | Chyd | Roth, Adamczak, et al., 1991 | liquid phase; ALS |
3 + C6H8 =
By formula: 3H2 + C6H8 = C6H14
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -432. ± 1. | kJ/mol | Chyd | Roth, Adamczak, et al., 1991 | liquid phase; ALS |
Henry's Law 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 by: Rolf Sander
Henry's Law constant (water solution)
kH(T) = k°H exp(d(ln(kH))/d(1/T) ((1/T) - 1/(298.15 K)))
k°H = Henry's law constant for solubility in water at 298.15 K (mol/(kg*bar))
d(ln(kH))/d(1/T) = Temperature dependence constant (K)
k°H (mol/(kg*bar)) | d(ln(kH))/d(1/T) (K) | Method | Reference | Comment |
---|---|---|---|---|
0.00076 | Q | N/A | missing citation give several references for the Henry's law constants but don't assign them to specific species. | |
0.0010 | 7500. | X | N/A | |
0.00060 | L | N/A | ||
0.00055 | V | N/A |
References
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Reaction thermochemistry data, Henry's Law 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]
Waddington G., 1947
Waddington G.,
Experimental vapor heat capacities and heats of vaporization of n-hexane and 2,2-dimethylbutane,
J. Am. Chem. Soc., 1947, 69, 2275-2279. [all data]
Douslin and Huffman, 1946
Douslin, D.R.; Huffman, H.M.,
Low-temperature thermal data on the five isometric hexanes,
J. Am. Chem. Soc., 1946, 68, 1704-1708. [all data]
Stull, 1937
Stull, D.R.,
A semi-micro calorimeter for measuring heat capacities at low temperatures,
J. Am. Chem. Soc., 1937, 59, 2726-2733. [all data]
Huffman, Parks, et al., 1931
Huffman, H.M.; Parks, G.S.; Barmore, M.,
Thermal data on organic compounds. X. Further studies on the heat capacities, entropies and free energies of hydrocarbons,
J. Am. Chem. Soc., 1931, 53, 3876-3888. [all data]
Parks, Huffman, et al., 1930
Parks, G.S.; Huffman, H.M.; Thomas, S.B.,
Thermal data on organic compounds. VI. The heat capacities, entropies and free energies of some saturated, non-benzenoid hydrocarbons,
J. Am. Chem. Soc., 1930, 52, 1032-1041. [all data]
Pruzan, 1991
Pruzan, P.,
Thermophysical properties of liquid n-hexane at temperatures from 243 K to 473 K and at pressures to 500 MPa,
J. Chem. Thermodynam., 1991, 23, 247-259. [all data]
Ohnishi, Fujihara, et al., 1989
Ohnishi, K.; Fujihara, I.; Murakami, S.,
Thermodynamic properties of decalins mixed with hexane isomers at 298.15K. 1. Excess enthalpies and excess isobaric heat capacities,
Fluid Phase Equilib., 1989, 46, 59-72. [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]
Perez-Casas, Aicart, et al., 1988
Perez-Casas, S.; Aicart, E.; Trojo, L.M.; Costas, M.,
Excess heat capacity. Chlorobenzene-2,2,4,4,6,8,8-heptamethylnonane, Int. Data Ser.,
Sel. Data Mixtures, 1988, (2)A, 123. [all data]
Saito and Tanaka, 1988
Saito, A.; Tanaka, R.,
Excess volumes and heat capacities of binary mixtures formed from cyclohexane, hexane and heptane at 298.15 K,
J. Chem. Thermodynam., 1988, 20, 859-865. [all data]
Benson and D'Arcy, 1986
Benson, G.C.; D'Arcy, P.J.,
Heat capacities of binary mixtures of n-octane with each of the hexane isomers at 298.15 K,
Can. J. Chem., 1986, 64, 2139-2141. [all data]
Naziev, Bashirov, et al., 1986
Naziev, Ya.M.; Bashirov, M.M.; Badalov, Yu.A.,
Experimental study of isobaric specific heat of higher alcohols at high pressures,
Inzh.-Fiz. Zhur., 1986, 51, 998-1004. [all data]
Tardajos, Aicart, et al., 1986
Tardajos, G.; Aicart, E.; Costas, M.; Patterson, D.,
Liquid structure and second-order mixing functions for benzene, toluene, and p-xylene with n-alkanes, J. Chem. Soc.,
Faraday Trans., 1986, 1 82, 2977-2987. [all data]
Costas and Patterson, 1985
Costas, M.; Patterson, D.,
Self-association of alcohols in inert solvents, J. Chem. Soc.,
Faraday Trans. 1, 1985, 81, 635-654. [all data]
Benson, D'Arcy, et al., 1984
Benson, G.C.; D'Arcy, P.J.; Kumaran, M.K.,
Heat capacities of binary mixtures of n-heptane with hexane isomers,
Thermochim. Acta, 1984, 75, 353-360. [all data]
Bravo, Pintos, et al., 1984
Bravo, R.; Pintos, M.; Baluja, M.C.; Paz Andrade, M.I.; Roux-Desgranges, G.; Grolier, J.-P.E.,
Excess volumes excess heat capacities of some mixtures: (an isomer of hexanol + an n-alkane) at 298.15 K,
J. Chem. Thermodynam., 1984, 16, 73-79. [all data]
Grigor'ev and Andolenko, 1984
Grigor'ev, B.A.; Andolenko, R.A.,
Investigation of the isobaric heat capacity of n-paraffinic hydrocarbons at atmospheric pressure, Izv. Vyssh. Ucheb. Zaved.,
Neft i Gaz, 1984, (2), 60-62. [all data]
Aicart, Kumaran, et al., 1983
Aicart, E.; Kumaran, M.K.; Halpin, C.J.; Benson, G.C.,
Ultrasonic speeds and isentropic compressibilities of 2-methylpentan-1-ol with hexane isomers at 298.15 K,
J. Chem. Thermodynam., 1983, 15, 1189-1197. [all data]
Benson, D'Arcy, et al., 1983
Benson, G.C.; D'Arcy, P.J.; Sugamori, M.E.,
Heat capacities of binary mixtures of 1-hexanol with hexane isomers at 298.15 K,
Thermochim. Acta, 1983, 71, 161-166. [all data]
Wilhelm, Inglese, et al., 1982
Wilhelm, E.; Inglese, A.; Quint, J.R.; Grolier, J.-P.E.,
Molar excess volumes and excess heat capacities of (1,2,4-trichlorobenzene + an alkane),
J. Chem. Thermodynam., 1982, 14, 303-308. [all data]
Zaripov, 1982
Zaripov, Z.I.,
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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 S°gas Entropy of gas at standard conditions S°liquid Entropy of liquid at standard conditions d(ln(kH))/d(1/T) Temperature dependence parameter for Henry's Law constant k°H Henry's Law constant at 298.15K 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 ΔrH° Enthalpy of reaction at standard conditions - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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