Cyclohexane
- Formula: C6H12
- Molecular weight: 84.1595
- IUPAC Standard InChIKey: XDTMQSROBMDMFD-UHFFFAOYSA-N
- CAS Registry Number: 110-82-7
- 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: Benzene, hexahydro-; Hexahydrobenzene; Hexamethylene; Hexanaphthene; Cicloesano; Cykloheksan; Rcra waste number U056; UN 1145; NSC 406835
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Gas phase thermochemistry data
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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 | -29.78 | kcal/mol | N/A | Spitzer and Huffman, 1947 | Value computed using ΔfHliquid° value of -157.7±1.8 kj/mol from Spitzer and Huffman, 1947 and ΔvapH° value of 33.1 kj/mol from Prosen, Johnson, et al., 1946.; DRB |
ΔfH°gas | -29.43 ± 0.19 | kcal/mol | Ccb | Prosen, Johnson, et al., 1946 | ALS |
ΔfH°gas | -29.47 | kcal/mol | N/A | Moore, Renquist, et al., 1940 | Value computed using ΔfHliquid° value of -156.4±1.3 kj/mol from Moore, Renquist, et al., 1940 and ΔvapH° value of 33.1 kj/mol from Prosen, Johnson, et al., 1946.; DRB |
Quantity | Value | Units | Method | Reference | Comment |
S°gas | 71.269 | cal/mol*K | N/A | Beckett C.W., 1947 | Close value of S(298.15 K)=298.78(0.75) J/mol*K was obtained by [43ASTSZA] from calorimetric data.; GT |
Constant pressure heat capacity of gas
Cp,gas (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
8.143 | 50. | Dorofeeva O.V., 1986 | There is an appreciable difference (up to 3.0-4.5 J/mol*K) between selected values of S(T) and Cp(T) and earlier statistically calculated values [ Brickwedde F.G., 1946, Beckett C.W., 1947, Kilpatrick J.E., 1947, Lippincott E.R., 1966] at high temperatures. It is due to using the most reliable molecular constants in [ Dorofeeva O.V., 1986].; GT |
10.18 | 100. | ||
13.10 | 150. | ||
16.50 | 200. | ||
22.75 | 273.15 | ||
25.18 ± 0.48 | 298.15 | ||
25.361 | 300. | ||
35.526 | 400. | ||
45.096 | 500. | ||
53.389 | 600. | ||
60.378 | 700. | ||
66.217 | 800. | ||
71.085 | 900. | ||
75.148 | 1000. | ||
78.552 | 1100. | ||
81.417 | 1200. | ||
83.841 | 1300. | ||
85.908 | 1400. | ||
87.679 | 1500. |
Constant pressure heat capacity of gas
Cp,gas (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
33.000 | 370. | Spitzer R., 1946 | Please also see Montgomery J.B., 1942.; GT |
34.21 ± 0.30 | 384. | ||
35.000 | 390. | ||
36.800 | 410. | ||
38.67 ± 0.40 | 428. | ||
41.70 ± 0.40 | 460. | ||
45.30 ± 0.50 | 495. | ||
47.00 ± 0.50 | 521. | ||
49.30 ± 0.50 | 544. |
Condensed phase thermochemistry data
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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 | -37.68 ± 0.42 | kcal/mol | Ccb | Spitzer and Huffman, 1947 | ALS |
ΔfH°liquid | -37.34 ± 0.19 | kcal/mol | Ccb | Prosen, Johnson, et al., 1946 | ALS |
ΔfH°liquid | -37.39 ± 0.32 | kcal/mol | Ccb | Moore, Renquist, et al., 1940 | Reanalyzed by Cox and Pilcher, 1970, Original value = -37.69 kcal/mol; ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -938. ± 5. | kcal/mol | AVG | N/A | Average of 7 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
S°liquid | 48.731 | cal/mol*K | N/A | Aston, Szasa, et al., 1943 | DH |
S°liquid | 48.841 | cal/mol*K | N/A | Ruehrwein and Huffman, 1943 | DH |
S°liquid | 49.21 | cal/mol*K | N/A | Parks, Huffman, et al., 1930 | Extrapolation below 90 K, 50.54 J/mol*K.; DH |
Constant pressure heat capacity of liquid
Cp,liquid (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
37.285 | 298.15 | Trejo, Costas, et al., 1991 | DH |
37.500 | 298.15 | Lainez, Rodrigo, et al., 1989 | DH |
34.39 | 326.5 | Voss and Sloan, 1989 | T = 326.5 to 450.0 K. Unsmoothed experimental datum.; DH |
37.275 | 298.15 | Saito and Tanaka, 1988 | DH |
36.883 | 298.15 | Shiohama, Ogawa, et al., 1988 | DH |
37.077 | 293.15 | Kalali, Kohler, et al., 1987 | T = 293.15, 313.15 K.; DH |
37.538 | 298.15 | Jimenez, Romani, et al., 1986 | DH |
37.249 | 298.15 | Ortega, 1986 | DH |
37.40 | 298.15 | Nkinamubanzi, Charlet, et al., 1985 | DH |
37.275 | 298.15 | Tanaka, Nakamichi, et al., 1985 | DH |
37.000 | 293.15 | Siddiqi, Svejda, et al., 1983 | DH |
37.38 | 298.15 | Grolier, Inglese, et al., 1982 | DH |
37.28 | 298.15 | Tanaka, 1982 | T = 293.15, 298.15, 303.15 K. Data at three temperatures.; DH |
37.3205 | 298.15 | Fortier, D'Arcy, et al., 1979 | DH |
37.314 | 298.15 | Vesely, Zabransky, et al., 1979 | DH |
37.38 | 298.15 | Wilhelm, Grolier, et al., 1979 | DH |
37.369 | 298.15 | Grolier, Wilhelm, et al., 1978 | DH |
37.45 | 298. | Safir, 1978 | T = 298 to 313 K. Data calculated from equation Cp = 1.7493 + 0.00452 T kJ/kg*K.; DH |
37.314 | 298.15 | Vesely, Svoboda, et al., 1977 | T = 298 to 318 K.; DH |
37.302 | 298.15 | Fortier, Benson, et al., 1976 | DH |
37.3016 | 298.15 | Fortier and Benson, 1976 | DH |
37.333 | 298.15 | Jolicoeur, Boileau, et al., 1975 | DH |
36.998 | 293.15 | Wilhelm, Zettler, et al., 1974 | T = 273 to 323 K.; DH |
38.15 | 298.15 | Subrahmanyam and Rajagopal, 1973 | T = 298 to 323 K.; DH |
37.09 | 298.15 | Wilhelm, Schano, et al., 1969 | Temperature 20, 30, and 40°C.; DH |
37.17 | 298. | Recko, 1968 | T = 24 to 40°C, equation only.; DH |
36.551 | 298. | Nikolaev, Rabinovich, et al., 1966 | T = 10 to 50°C.; DH |
37.120 | 298.00 | Moelwyn-Hughes and Thorpe, 1964 | T = 297 to 327 K.; DH |
37.09 | 311. | Swietoslawski and Zielenkiewicz, 1960 | Mean value 20 to 56°C.; DH |
36.85 | 300. | Auerbach, Sage, et al., 1950 | T = 300 to 366 K. Cp given as 0.4378 Btu/lb*R at 80°F.; DH |
37.249 | 295. | Aston, Szasa, et al., 1943 | T = 12 to 293 K.; DH |
37.359 | 298.15 | Ruehrwein and Huffman, 1943 | T = 13 to 302 K.; DH |
24.00 | 304.2 | Phillip, 1939 | DH |
34.39 | 298.9 | Parks, Huffman, et al., 1930 | T = 92 to 299 K. Value is unsmoothed experimental datum.; DH |
42.09 | 298. | Dejardin, 1919 | T = 22 to 50°C.; DH |
Reaction thermochemistry data
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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
M - Michael M. Meot-Ner (Mautner) and Sharon G. Lias
B - John E. Bartmess
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: C6H10 + H2 = C6H12
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -28. ± 1. | kcal/mol | AVG | N/A | Average of 8 values; Individual data points |
By formula: H4N+ + C6H12 = (H4N+ • C6H12)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 9. | kcal/mol | PHPMS | Deakyne and Meot-Ner (Mautner), 1985 | gas phase; Entropy change calculated or estimated, DG<, ΔrH<; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 20. | cal/mol*K | N/A | Deakyne and Meot-Ner (Mautner), 1985 | gas phase; Entropy change calculated or estimated, DG<, ΔrH<; M |
Free energy of reaction
ΔrG° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
2.8 | 317. | PHPMS | Deakyne and Meot-Ner (Mautner), 1985 | gas phase; Entropy change calculated or estimated, DG<, ΔrH<; M |
By formula: C6H6+ + C6H12 = (C6H6+ • C6H12)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 11.2 | kcal/mol | PHPMS | Meot-Ner (Mautner), Hamlet, et al., 1978 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 27. | cal/mol*K | N/A | Meot-Ner (Mautner), Hamlet, et al., 1978 | gas phase; Entropy change calculated or estimated; M |
Free energy of reaction
ΔrG° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
3.2 | 295. | PHPMS | Meot-Ner (Mautner), Hamlet, et al., 1978 | gas phase; Entropy change calculated or estimated; M |
C6H11- + =
By formula: C6H11- + H+ = C6H12
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 418.3 ± 2.0 | kcal/mol | Bran | Peerboom, Rademaker, et al., 1992 | gas phase; B |
ΔrH° | 406.82 ± 0.90 | kcal/mol | G+TS | Bohme, Lee-Ruff, et al., 1972 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 409.5 ± 2.2 | kcal/mol | H-TS | Peerboom, Rademaker, et al., 1992 | gas phase; B |
ΔrG° | >398.00 | kcal/mol | IMRB | Bohme, Lee-Ruff, et al., 1972 | gas phase; B |
By formula: 2H2 + C6H8 = C6H12
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -53.64 ± 0.29 | kcal/mol | Chyd | Turner, Mallon, et al., 1973 | liquid phase; solvent: Glacial acetic acid; ALS |
ΔrH° | -54.88 ± 0.10 | kcal/mol | Chyd | Kistiakowsky, Ruhoff, et al., 1936 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -55.4 ± 0.1 kcal/mol; At 355 °K; ALS |
By formula: 2H2 + C6H8 = C6H12
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -55.6 | kcal/mol | Chyd | Roth, Adamczak, et al., 1991 | liquid phase; ALS |
ΔrH° | -53.90 ± 0.33 | kcal/mol | Chyd | Turner, Mallon, et al., 1973 | liquid phase; solvent: Glacial acetic acid; ALS |
By formula: C3H9Si+ + C6H12 = (C3H9Si+ • C6H12)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 37.9 | kcal/mol | PHPMS | Li and Stone, 1989 | gas phase; condensation; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 48.1 | cal/mol*K | PHPMS | Li and Stone, 1989 | gas phase; condensation; M |
By formula: 3H2 + C6H6 = C6H12
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -49.06 ± 0.15 | kcal/mol | Chyd | Kistiakowsky, Ruhoff, et al., 1936 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -49.80 ± 0.15 kcal/mol; At 355 °K; ALS |
By formula: HI + C6H11I = C6H12 + I2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -7.8 ± 2.0 | kcal/mol | Cm | Brennan and Ubbelohde, 1956 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -6.8 ± 1.0 kcal/mol; ALS |
By formula: Li+ + C6H12 = (Li+ • C6H12)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 24. | kcal/mol | ICR | Staley and Beauchamp, 1975 | gas phase; switching reaction(Li+)H2O, from graph; Dzidic and Kebarle, 1970 extrapolated; M |
By formula: C6H12 = C6H12
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -3.510 | kcal/mol | Eqk | Glasebrook and Lovell, 1939 | liquid phase; Heat of isomerization; ALS |
By formula: 2H2 + C6H8 = C6H12
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -102.0 ± 1.9 | kcal/mol | Chyd | Roth, Adamczak, et al., 1991 | liquid phase; ALS |
By formula: C6H12O = C6H12 + H2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 15.2 ± 0.55 | kcal/mol | Eqk | Fedoseenko, Yursha, et al., 1983 | gas phase; At 502 K; ALS |
By formula: C6H11Cl + HCl = C6H12 + Cl2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -34.20 | kcal/mol | Cm | Kirkbride, 1956 | liquid phase; ALS |
By formula: C6H12 = C6H12
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 4.32 ± 0.28 | kcal/mol | Eqk | Kabo and Andreevskii, 1973 | liquid phase; ALS |
Henry's Law data
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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 |
---|---|---|---|---|
0.0051 | Q | N/A | missing citation give several references for the Henry's law constants but don't assign them to specific species. | |
0.0055 | 3200. | X | N/A | |
0.0062 | 710. | X | N/A | |
0.0056 | L | N/A | ||
0.0051 | V | N/A |
Vibrational and/or electronic energy levels
Go To: Top, Gas phase thermochemistry data, 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 by: Takehiko Shimanouchi
Symmetry: D3d Symmetry Number σ = 6
Sym. | No | Approximate | Selected Freq. | Infrared | Raman | Comments | ||||
---|---|---|---|---|---|---|---|---|---|---|
Species | type of mode | Value | Rating | Value | Phase | Value | Phase | |||
a1g | 1 | CH2 a-str | 2930 | E | ia | 2938 VS p | liq. | FR(2ν3) | ||
a1g | 1 | CH2 a-str | 2930 | E | ia | 2923 VS p | liq. | FR(2ν3) | ||
a1g | 2 | CH2 s-str | 2852 | C | ia | 2852 VS p | liq. | |||
a1g | 3 | CH2 scis | 1465 | C | ia | 1465 M p | liq. | |||
a1g | 4 | CH2 rock | 1157 | C | ia | 1157 S p | liq. | |||
a1g | 5 | CC str | 802 | C | ia | 802 VS p | liq. | |||
a1g | 6 | CCC deform + CC torsion | 383 | C | ia | 383 M p | liq. | |||
a1u | 7 | CH2 twist | 1383 | C | 1383 | gas | ia | Observed in the crystalline state at about ν90 K | ||
a1u | 8 | CH2 wag | 1157 | C | 1157 | gas | ia | Observed in the crystalline state at about ν90 K | ||
a1u | 9 | CC str + CC torsion | 1057 | C | 1057 | gas | ia | Observed in the crystalline state at about ν90 K | ||
a2g | 10 | CH2 wag | 1437 | C | 1437 | gas | ia | Observed in the crystalline state at about ν90 K | ||
a2g | 11 | CH2 twist | 1090 | C | 1090 | gas | ia | Observed in the crystalline state at about ν90 K | ||
a2u | 12 | CH2 a-str | 2915 | E | 2915 M | gas | ia | |||
a2u | 13 | CH2 s-str | 2860 | E | ia | SF(ν2,ν18,ν26) | ||||
a2u | 14 | CH2 scis | 1437 | C | 1437 M | gas | ia | |||
a2u | 15 | CH2 rock | 1030 | D | 1040 M | gas | ia | FR(ν23+ν32) | ||
a2u | 15 | CH2 rock | 1030 | D | 1016 M | gas | ia | FR(ν23+ν32) | ||
a2u | 16 | CCC deform | 523 | A | 523 W | gas | ia | |||
eg | 17 | CH2 a-str | 2930 | E | ia | SF(ν1,ν12,ν25) | ||||
eg | 18 | CH2 s-str | 2897 | E | ia | 2897 M vb | ||||
eg | 19 | CH2 scis | 1443 | C | ia | 1443 S dp | ||||
eg | 20 | CH2 wag | 1347 | C | ia | 1347 S dp | ||||
eg | 21 | CH2 twist | 1266 | C | ia | 1266 VS dp | ||||
eg | 22 | CC str | 1027 | C | ia | 1027 VS dp | ||||
eg | 23 | CH2 rock | 785 | C | 785 | gas | 785 VW dp | liq. | Observed in the crystalline state at about ν90 K | |
eg | 24 | CCC deform + CC torsion | 426 | C | ia | 426 S dp | liq. | |||
eu | 25 | CH2 a-str | 2933 | A | 2933 VS | gas | ia | |||
eu | 26 | CH2 s-str | 2863 | A | 2863 VS | gas | ia | |||
eu | 27 | CH2 scis | 1457 | A | 1457 VS | gas | ia | |||
eu | 28 | CH2 wag | 1355 | B | 1355 W | gas | ia | |||
eu | 29 | CH2 twist | 1261 | A | 1261 S | gas | ia | |||
eu | 30 | CH2 rock | 907 | B | 907 S | gas | ia | |||
eu | 31 | CC str | 863 | A | 863 S | gas | ia | |||
eu | 32 | CCC deform + CC torsion | 248 | C | 248 VW | liq. | ia | |||
Source: Shimanouchi, 1972
Notes
VS | Very strong |
S | Strong |
M | Medium |
W | Weak |
VW | Very weak |
ia | Inactive |
vb | Very broad |
p | Polarized |
dp | Depolarized |
FR | Fermi resonance with an overtone or a combination tone indicated in the parentheses. |
SF | Calculation shows that the frequency approximately equals that of the vibration indicated in the parentheses. |
A | 0~1 cm-1 uncertainty |
B | 1~3 cm-1 uncertainty |
C | 3~6 cm-1 uncertainty |
D | 6~15 cm-1 uncertainty |
E | 15~30 cm-1 uncertainty |
References
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Reaction thermochemistry data, Henry's Law data, Vibrational and/or electronic energy levels, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Spitzer and Huffman, 1947
Spitzer, R.; Huffman, H.M.,
The heats of combustion of cyclopentane, cyclohexane, cycloheptane and cyclooctane,
J. Am. Chem. Soc., 1947, 69, 211-213. [all data]
Prosen, Johnson, et al., 1946
Prosen, E.J.; Johnson, W.H.; Rossini, F.D.,
Heats of formation and combustion of the normal alkylcyclopentanes and cyclohexanes and the increment per CH2 group for several homologous series of hydrocarbons,
J. Res. NBS, 1946, 37, 51-56. [all data]
Moore, Renquist, et al., 1940
Moore, G.E.; Renquist, M.L.; Parks, G.S.,
Thermal data on organic compounds. XX. Modern combustion data for two methylnonanes, methyl ethyl ketone, thiophene and six cycloparaffins,
J. Am. Chem. Soc., 1940, 62, 1505-1507. [all data]
Beckett C.W., 1947
Beckett C.W.,
The thermodynamic properties and molecular structure of cyclohexane, methylcyclohexane, ethylcyclohexane, and seven dimethylcyclohexanes,
J. Am. Chem. Soc., 1947, 69, 2488-2495. [all data]
Dorofeeva O.V., 1986
Dorofeeva O.V.,
Thermodynamic properties of twenty-one monocyclic hydrocarbons,
J. Phys. Chem. Ref. Data, 1986, 15, 437-464. [all data]
Brickwedde F.G., 1946
Brickwedde F.G.,
Equilibrium constants of some reactions involved in the production of 1,3-butadiene,
J. Res. Nat. Bur. Stand., 1946, 37, 263-279. [all data]
Kilpatrick J.E., 1947
Kilpatrick J.E.,
Heats, equilibrium constants, and free energies of formation of the alkylcyclopentanes and alkylcyclohexanes,
J. Res. Nat. Bur. Stand., 1947, 39, 523-543. [all data]
Lippincott E.R., 1966
Lippincott E.R.,
Enthalpy, free energy, entropy, and heat capacity of cyclohexane and acetaldehyde,
Bull. Soc. Chim. Belges., 1966, 75, 655-667. [all data]
Spitzer R., 1946
Spitzer R.,
The heat capacity of gaseous cyclopentane, cyclohexane and methylcyclohexane,
J. Am. Chem. Soc., 1946, 68, 2537-2538. [all data]
Montgomery J.B., 1942
Montgomery J.B.,
The heat capacity of organic vapors. IV. Benzene, fluorobenzene, toluene, cyclohexane, methylcyclohexane and cyclohexene,
J. Am. Chem. Soc., 1942, 64, 2375-2377. [all data]
Cox and Pilcher, 1970
Cox, J.D.; Pilcher, G.,
Thermochemistry of Organic and Organometallic Compounds, Academic Press, New York, 1970, 1-636. [all data]
Aston, Szasa, et al., 1943
Aston, J.G.; Szasa, G.J.; Fink, H.L.,
The heat capacity and entropy, heats of transition, fusion and vaporization and the vapor pressures of cyclohexane. The vibrational frequencies of alicyclic ring systems,
J. Am. Chem. Soc., 1943, 65, 1135-1139. [all data]
Ruehrwein and Huffman, 1943
Ruehrwein, R.A.; Huffman, H.M.,
Thermal data. XVII. The heat capacity, entropy and free energy of formation of cyclohexane. A new method of heat transfer in low temperature calorimetry,
J. Am. Chem. Soc., 1943, 65, 1620-1625. [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]
Trejo, Costas, et al., 1991
Trejo, L.M.; Costas, M.; Patterson, D.,
Excess heat capacity of organic mixtures, Internat. DATA Series,
Selected Data Mixt., 1991, Ser. [all data]
Lainez, Rodrigo, et al., 1989
Lainez, A.; Rodrigo, M.M.; Wilhelm, E.; Grolier, J.-P.E.,
Excess volumes and excess heaat capacitiies of some mixtures with trans,trans,cis-1,5,9-cyclododecatriene at 298.15K,
J. Chem. Eng. Data, 1989, 34, 332-335. [all data]
Voss and Sloan, 1989
Voss, S.F.; Sloan, E.D.,
Thermal conductivity and heat capacity of synthetic fuel components,
Int. J. Thermophys., 1989, 10(5), 1029-1040. [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]
Shiohama, Ogawa, et al., 1988
Shiohama, Y.; Ogawa, H.; Murakami, S.; Fujihara, I.,
Excess thermodynamic properties of (cis-decalin or trans-decalin + cyclohexane or methylcyclohexane or cyclooctane) at 298.15 K,
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Determination of excess heat capacities of (benzene + tetrachloromethane and + cyclohexane) between 293.15 and 303.15 K by use of a Picker flow calorimeter,
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Heat capacities of binary cycloalkane mixtures at 298.15 K,
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Recko, 1968
Recko, W.M.,
Excess heat capacity of the binary systems formed by n-propyl alcohol with benzene, mesitylene and cyclohexane,
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Nikolaev, Rabinovich, et al., 1966
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Moelwyn-Hughes and Thorpe, 1964
Moelwyn-Hughes, E.A.; Thorpe, P.L.,
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Swietoslawski and Zielenkiewicz, 1960
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Isobaric heat capacities at bubble point,
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Adiabatic and isothermal compressibilities of liquids,
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Dejardin, 1919
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Acidity order of selected bronsted acids in the gas phase at 300K,
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Turner, Mallon, et al., 1973
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Staley and Beauchamp, 1975
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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 T Temperature 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 ΔrG° Free energy of reaction at standard conditions ΔrH° Enthalpy of reaction at standard conditions ΔrS° Entropy of reaction at standard conditions - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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