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
- Permanent link for this species. Use this link for bookmarking this species for future reference.
- Information on this page:
- Gas phase thermochemistry data
- Condensed phase thermochemistry data
- Phase change data
- Reaction thermochemistry data
- Henry's Law data
- Gas phase ion energetics data
- Ion clustering data
- IR Spectrum
- Mass spectrum (electron ionization)
- UV/Visible spectrum
- Vibrational and/or electronic energy levels
- References
- Notes
- Other data available:
- Data at other public NIST sites:
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Gas phase thermochemistry data
Go To: Top, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, Gas phase ion energetics data, Ion clustering data, IR Spectrum, Mass spectrum (electron ionization), UV/Visible spectrum, Vibrational and/or electronic energy levels, 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 | -124.6 | kJ/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 | -123.1 ± 0.79 | kJ/mol | Ccb | Prosen, Johnson, et al., 1946 | ALS |
ΔfH°gas | -123.3 | kJ/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 | 298.19 | J/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 (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
34.07 | 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 |
42.59 | 100. | ||
54.80 | 150. | ||
69.05 | 200. | ||
95.20 | 273.15 | ||
105.3 ± 2.0 | 298.15 | ||
106.11 | 300. | ||
148.64 | 400. | ||
188.68 | 500. | ||
223.38 | 600. | ||
252.62 | 700. | ||
277.05 | 800. | ||
297.42 | 900. | ||
314.42 | 1000. | ||
328.66 | 1100. | ||
340.65 | 1200. | ||
350.79 | 1300. | ||
359.44 | 1400. | ||
366.85 | 1500. |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
138.07 | 370. | Spitzer R., 1946 | Please also see Montgomery J.B., 1942.; GT |
143.1 ± 1.3 | 384. | ||
146.44 | 390. | ||
153.97 | 410. | ||
161.8 ± 1.7 | 428. | ||
174.5 ± 1.7 | 460. | ||
189.5 ± 2.1 | 495. | ||
196.7 ± 2.1 | 521. | ||
206.3 ± 2.1 | 544. |
Condensed phase thermochemistry data
Go To: Top, Gas phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, Gas phase ion energetics data, Ion clustering data, IR Spectrum, Mass spectrum (electron ionization), UV/Visible spectrum, Vibrational and/or electronic energy levels, 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 | -157.7 ± 1.8 | kJ/mol | Ccb | Spitzer and Huffman, 1947 | ALS |
ΔfH°liquid | -156.2 ± 0.79 | kJ/mol | Ccb | Prosen, Johnson, et al., 1946 | ALS |
ΔfH°liquid | -156.4 ± 1.3 | kJ/mol | Ccb | Moore, Renquist, et al., 1940 | Reanalyzed by Cox and Pilcher, 1970, Original value = -157.7 kJ/mol; ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -3930. ± 20. | kJ/mol | AVG | N/A | Average of 7 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
S°liquid | 203.89 | J/mol*K | N/A | Aston, Szasa, et al., 1943 | DH |
S°liquid | 204.35 | J/mol*K | N/A | Ruehrwein and Huffman, 1943 | DH |
S°liquid | 205.9 | J/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 (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
156.00 | 298.15 | Trejo, Costas, et al., 1991 | DH |
156.90 | 298.15 | Lainez, Rodrigo, et al., 1989 | DH |
143.9 | 326.5 | Voss and Sloan, 1989 | T = 326.5 to 450.0 K. Unsmoothed experimental datum.; DH |
155.96 | 298.15 | Saito and Tanaka, 1988 | DH |
154.32 | 298.15 | Shiohama, Ogawa, et al., 1988 | DH |
155.13 | 293.15 | Kalali, Kohler, et al., 1987 | T = 293.15, 313.15 K.; DH |
157.06 | 298.15 | Jimenez, Romani, et al., 1986 | DH |
155.85 | 298.15 | Ortega, 1986 | DH |
156.5 | 298.15 | Nkinamubanzi, Charlet, et al., 1985 | DH |
155.96 | 298.15 | Tanaka, Nakamichi, et al., 1985 | DH |
154.81 | 293.15 | Siddiqi, Svejda, et al., 1983 | DH |
156.4 | 298.15 | Grolier, Inglese, et al., 1982 | DH |
156.0 | 298.15 | Tanaka, 1982 | T = 293.15, 298.15, 303.15 K. Data at three temperatures.; DH |
156.149 | 298.15 | Fortier, D'Arcy, et al., 1979 | DH |
156.12 | 298.15 | Vesely, Zabransky, et al., 1979 | DH |
156.4 | 298.15 | Wilhelm, Grolier, et al., 1979 | DH |
156.35 | 298.15 | Grolier, Wilhelm, et al., 1978 | DH |
156.7 | 298. | Safir, 1978 | T = 298 to 313 K. Data calculated from equation Cp = 1.7493 + 0.00452 T kJ/kg*K.; DH |
156.12 | 298.15 | Vesely, Svoboda, et al., 1977 | T = 298 to 318 K.; DH |
156.07 | 298.15 | Fortier, Benson, et al., 1976 | DH |
156.070 | 298.15 | Fortier and Benson, 1976 | DH |
156.20 | 298.15 | Jolicoeur, Boileau, et al., 1975 | DH |
154.80 | 293.15 | Wilhelm, Zettler, et al., 1974 | T = 273 to 323 K.; DH |
159.6 | 298.15 | Subrahmanyam and Rajagopal, 1973 | T = 298 to 323 K.; DH |
155.2 | 298.15 | Wilhelm, Schano, et al., 1969 | Temperature 20, 30, and 40°C.; DH |
155.5 | 298. | Recko, 1968 | T = 24 to 40°C, equation only.; DH |
152.93 | 298. | Nikolaev, Rabinovich, et al., 1966 | T = 10 to 50°C.; DH |
155.31 | 298.00 | Moelwyn-Hughes and Thorpe, 1964 | T = 297 to 327 K.; DH |
155.2 | 311. | Swietoslawski and Zielenkiewicz, 1960 | Mean value 20 to 56°C.; DH |
154.2 | 300. | Auerbach, Sage, et al., 1950 | T = 300 to 366 K. Cp given as 0.4378 Btu/lb*R at 80°F.; DH |
155.85 | 295. | Aston, Szasa, et al., 1943 | T = 12 to 293 K.; DH |
156.31 | 298.15 | Ruehrwein and Huffman, 1943 | T = 13 to 302 K.; DH |
100.4 | 304.2 | Phillip, 1939 | DH |
143.9 | 298.9 | Parks, Huffman, et al., 1930 | T = 92 to 299 K. Value is unsmoothed experimental datum.; DH |
176.1 | 298. | Dejardin, 1919 | T = 22 to 50°C.; DH |
Phase change data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Reaction thermochemistry data, Henry's Law data, Gas phase ion energetics data, Ion clustering data, IR Spectrum, Mass spectrum (electron ionization), UV/Visible spectrum, Vibrational and/or electronic energy levels, 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
DRB - Donald R. Burgess, Jr.
DH - Eugene S. Domalski and Elizabeth D. Hearing
CAL - James S. Chickos, William E. Acree, Jr., Joel F. Liebman, Students of Chem 202 (Introduction to the Literature of Chemistry), University of Missouri -- St. Louis
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 353.9 ± 0.2 | K | AVG | N/A | Average of 93 out of 116 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 279.6 ± 0.3 | K | AVG | N/A | Average of 38 out of 47 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 279.7 ± 0.4 | K | AVG | N/A | Average of 8 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 554. ± 1. | K | AVG | N/A | Average of 18 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 40.7 ± 0.5 | bar | AVG | N/A | Average of 8 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Vc | 0.308 | l/mol | N/A | Daubert, 1996 | |
Vc | 0.309 | l/mol | N/A | Young, 1972 | Uncertainty assigned by TRC = 0.003 l/mol; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 3.24 ± 0.03 | mol/l | N/A | Daubert, 1996 | |
ρc | 3.26 | mol/l | N/A | Teja and Anselme, 1990 | Uncertainty assigned by TRC = 0.07 mol/l; TRC |
ρc | 3.230 | mol/l | N/A | Simon, 1957 | Uncertainty assigned by TRC = 0.04 mol/l; TRC |
ρc | 3.250 | mol/l | N/A | Young, 1910 | Uncertainty assigned by TRC = 0.02 mol/l; TRC |
ρc | 3.247 | mol/l | N/A | Young and Fortey, 1899 | Uncertainty assigned by TRC = 0.06 mol/l; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 33.1 ± 0.4 | kJ/mol | AVG | N/A | Average of 19 out of 21 values; Individual data points |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
29.97 | 353.9 | N/A | Majer and Svoboda, 1985 | |
33.334 | 298.15 | N/A | Aston, Szasa, et al., 1943 | P = 13.18 kPa; DH |
33.1 | 315. | EB | Gierycz, Kosowski, et al., 2009 | Based on data from 296. to 353. K.; AC |
32.7 | 315. | N/A | Lubomska, Banas, et al., 2002 | Based on data from 300. to 345. K.; AC |
31.9 | 324. | EB | Diogo, Santos, et al., 1995 | Based on data from 313. to 336. K.; AC |
32.2 | 375. | N/A | Lee and Holder, 1993 | Based on data from 360. to 470. K.; AC |
32.3 | 314. | C | Dong, Lin, et al., 1988 | AC |
31.1 | 332. | C | Dong, Lin, et al., 1988 | AC |
30.3 | 345. | C | Dong, Lin, et al., 1988 | AC |
30.0 | 355. | C | Dong, Lin, et al., 1988 | AC |
30.9 | 368. | A | Stephenson and Malanowski, 1987 | Based on data from 353. to 414. K.; AC |
29.6 | 427. | A | Stephenson and Malanowski, 1987 | Based on data from 412. to 491. K.; AC |
29.6 | 504. | A | Stephenson and Malanowski, 1987 | Based on data from 489. to 553. K.; AC |
32.9 | 308. | A,MM | Stephenson and Malanowski, 1987 | Based on data from 293. to 355. K. See also Willingham, Taylor, et al., 1945.; AC |
32.3 ± 0.1 | 313. | C | Majer, Svoboda, et al., 1979 | AC |
31.2 ± 0.1 | 333. | C | Majer, Svoboda, et al., 1979 | AC |
31.0 ± 0.1 | 338. | C | Majer, Svoboda, et al., 1979 | AC |
30.4 ± 0.1 | 348. | C | Majer, Svoboda, et al., 1979 | AC |
30.1 ± 0.1 | 353. | C | Majer, Svoboda, et al., 1979 | AC |
32.2 ± 0.1 | 313. | C | Svoboda, Veselý, et al., 1973 | AC |
31.9 ± 0.1 | 323. | C | Svoboda, Veselý, et al., 1973 | AC |
31.1 ± 0.1 | 333. | C | Svoboda, Veselý, et al., 1973 | AC |
30.6 ± 0.1 | 343. | C | Svoboda, Veselý, et al., 1973 | AC |
30.1 ± 0.1 | 354. | C | Svoboda, Veselý, et al., 1973 | AC |
32.5 | 318. | N/A | Gaw and Swinton, 1968 | Based on data from 303. to 343. K.; AC |
32.9 | 313. | N/A | Cruickshank and Cutler, 1967 | Based on data from 298. to 348. K.; AC |
32.8 | 331. | N/A | Marinichev and Susarev, 1965 | Based on data from 316. to 354. K.; AC |
31.4 ± 0.1 | 324. | C | McCullough, Person, et al., 1951 | AC |
30.4 ± 0.1 | 346. | C | McCullough, Person, et al., 1951 | AC |
30.1 | 354. | N/A | Spitzer and Pitzer, 1946 | 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)
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Temperature (K) | 292. to 422. |
---|---|
A (kJ/mol) | 43.32 |
α | -0.1437 |
β | 0.4512 |
Tc (K) | 553.4 |
Reference | Majer and Svoboda, 1985 |
Entropy of vaporization
ΔvapS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
111.80 | 298.15 | Aston, Szasa, et al., 1943 | P; DH |
Antoine Equation Parameters
log10(P) = A − (B / (T + C))
P = vapor pressure (bar)
T = temperature (K)
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Temperature (K) | A | B | C | Reference | Comment |
---|---|---|---|---|---|
323. to 523. | 4.13983 | 1316.554 | -35.581 | Kerns, Anthony, et al., 1974 | Coefficents calculated by NIST from author's data. |
303. to 343. | 3.9920 | 1216.93 | -48.621 | Gaw and Swinton, 1968, 2 | Coefficents calculated by NIST from author's data. |
315.70 to 353.90 | 3.17125 | 780.637 | -107.29 | Marinichev and Susarev, 1965, 2 | Coefficents calculated by NIST from author's data. |
293.06 to 354.73 | 3.96988 | 1203.526 | -50.287 | Williamham, Taylor, et al., 1945 |
Enthalpy of sublimation
ΔsubH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
27.6 | 265. | A | Stephenson and Malanowski, 1987 | Based on data from 223. to 280. K.; AC |
46.6 | 186. | B | Bondi, 1963 | AC |
37.2 | 273. | N/A | Jones, 1960 | Based on data from 268. to 278. K.; AC |
37.7 | 248. | A | Stull, 1947 | Based on data from 228. to 268. K.; AC |
36.5 | 274. | A | Rotinjanz and Nagornow, 1934 | Based on data from 269. to 279. K.; AC |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
2.68 | 279.8 | Domalski and Hearing, 1996 | AC |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
36.2 | 186.1 | Domalski and Hearing, 1996 | CAL |
9.57 | 279.8 |
Enthalpy of phase transition
ΔHtrs (kJ/mol) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
6.686 | 186.09 | crystaline, II | crystaline, I | Aston, Szasa, et al., 1943 | DH |
2.628 | 279.84 | crystaline, I | liquid | Aston, Szasa, et al., 1943 | DH |
6.7396 | 186.1 | crystaline, II | crystaline, I | Ruehrwein and Huffman, 1943 | DH |
2.6769 | 279.82 | crystaline, I | liquid | Ruehrwein and Huffman, 1943 | DH |
6.820 | 186.4 | crystaline, II | crystaline, I | Ziegler and Andrews, 1942 | DH |
2.728 | 279.4 | crystaline, I | liquid | Ziegler and Andrews, 1942 | DH |
6.234 | 185.9 | crystaline, II | crystaline, I | Parks, Huffman, et al., 1930 | DH |
2.423 | 279.3 | crystaline, I | liquid | Parks, Huffman, et al., 1930 | DH |
Entropy of phase transition
ΔStrs (J/mol*K) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
35.93 | 186.09 | crystaline, II | crystaline, I | Aston, Szasa, et al., 1943 | DH |
9.39 | 279.84 | crystaline, I | liquid | Aston, Szasa, et al., 1943 | DH |
36.21 | 186.1 | crystaline, II | crystaline, I | Ruehrwein and Huffman, 1943 | DH |
9.57 | 279.82 | crystaline, I | liquid | Ruehrwein and Huffman, 1943 | DH |
36.59 | 186.4 | crystaline, II | crystaline, I | Ziegler and Andrews, 1942 | DH |
9.76 | 279.4 | crystaline, I | liquid | Ziegler and Andrews, 1942 | DH |
33.53 | 185.9 | crystaline, II | crystaline, I | Parks, Huffman, et al., 1930 | DH |
8.68 | 279.3 | crystaline, I | liquid | Parks, Huffman, et al., 1930 | DH |
Reaction thermochemistry data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics data, Ion clustering data, IR Spectrum, Mass spectrum (electron ionization), UV/Visible spectrum, Vibrational and/or electronic energy levels, 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
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° | -118. ± 6. | kJ/mol | AVG | N/A | Average of 8 values; Individual data points |
By formula: H4N+ + C6H12 = (H4N+ • C6H12)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 40. | kJ/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° | 84. | J/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° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
12. | 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° | 46.9 | kJ/mol | PHPMS | Meot-Ner (Mautner), Hamlet, et al., 1978 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 110. | J/mol*K | N/A | Meot-Ner (Mautner), Hamlet, et al., 1978 | gas phase; Entropy change calculated or estimated; M |
Free energy of reaction
ΔrG° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
13. | 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° | 1750. ± 8.4 | kJ/mol | Bran | Peerboom, Rademaker, et al., 1992 | gas phase; B |
ΔrH° | 1702.1 ± 3.8 | kJ/mol | G+TS | Bohme, Lee-Ruff, et al., 1972 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1713. ± 9.2 | kJ/mol | H-TS | Peerboom, Rademaker, et al., 1992 | gas phase; B |
ΔrG° | >1665.2 | kJ/mol | IMRB | Bohme, Lee-Ruff, et al., 1972 | gas phase; B |
By formula: 2H2 + C6H8 = C6H12
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -224.4 ± 1.2 | kJ/mol | Chyd | Turner, Mallon, et al., 1973 | liquid phase; solvent: Glacial acetic acid; ALS |
ΔrH° | -229.6 ± 0.42 | kJ/mol | Chyd | Kistiakowsky, Ruhoff, et al., 1936 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -231.7 ± 0.4 kJ/mol; At 355 °K; ALS |
By formula: 2H2 + C6H8 = C6H12
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -233. | kJ/mol | Chyd | Roth, Adamczak, et al., 1991 | liquid phase; ALS |
ΔrH° | -225.5 ± 1.4 | kJ/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° | 159. | kJ/mol | PHPMS | Li and Stone, 1989 | gas phase; condensation; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 201. | J/mol*K | PHPMS | Li and Stone, 1989 | gas phase; condensation; M |
By formula: 3H2 + C6H6 = C6H12
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -205.3 ± 0.63 | kJ/mol | Chyd | Kistiakowsky, Ruhoff, et al., 1936 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -208.4 ± 0.63 kJ/mol; At 355 °K; ALS |
By formula: HI + C6H11I = C6H12 + I2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -32.6 ± 8.4 | kJ/mol | Cm | Brennan and Ubbelohde, 1956 | gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -28. ± 4.2 kJ/mol; ALS |
By formula: Li+ + C6H12 = (Li+ • C6H12)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 100. | kJ/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° | -14.69 | kJ/mol | Eqk | Glasebrook and Lovell, 1939 | liquid phase; Heat of isomerization; ALS |
By formula: 2H2 + C6H8 = C6H12
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -426.8 ± 7.9 | kJ/mol | Chyd | Roth, Adamczak, et al., 1991 | liquid phase; ALS |
By formula: C6H12O = C6H12 + H2
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 63.4 ± 2.3 | kJ/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° | -143.1 | kJ/mol | Cm | Kirkbride, 1956 | liquid phase; ALS |
By formula: C6H12 = C6H12
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 18.1 ± 1.2 | kJ/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 |
Gas phase ion energetics 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 evaluated as indicated in comments:
HL - Edward P. Hunter and Sharon G. Lias
L - Sharon G. Lias
Data compiled as indicated in comments:
B - John E. Bartmess
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
View reactions leading to C6H12+ (ion structure unspecified)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
IE (evaluated) | 9.88 ± 0.03 | eV | N/A | N/A | L |
Quantity | Value | Units | Method | Reference | Comment |
Proton affinity (review) | 686.9 | kJ/mol | N/A | Hunter and Lias, 1998 | HL |
Quantity | Value | Units | Method | Reference | Comment |
Gas basicity | 666.9 | kJ/mol | N/A | Hunter and Lias, 1998 | HL |
Ionization energy determinations
IE (eV) | Method | Reference | Comment |
---|---|---|---|
9.80 ± 0.05 | EI | Holmes and Lossing, 1991 | LL |
10.0 ± 0.03 | EI | Arimura and Yoshikawa, 1984 | LBLHLM |
9.82 | EQ | Sieck and Mautner(Meot-Ner), 1982 | LBLHLM |
9.88 ± 0.10 | EQ | Lias, 1982 | LBLHLM |
9.88 | PE | Kovac and Klasinc, 1978 | LLK |
9.88 ± 0.02 | PE | Bieri, Burger, et al., 1977 | LLK |
9.88 | EI | Lossing and Traeger, 1975 | LLK |
9.89 ± 0.01 | PE | Rang, Paldoia, et al., 1974 | LLK |
9.83 ± 0.05 | EI | Puttemans, 1974 | LLK |
9.84 | PE | Puttemans, 1974 | LLK |
9.88 ± 0.01 | PI | Sergeev, Akopyan, et al., 1973 | LLK |
9.87 | PE | Ikuta, Yoshihara, et al., 1973 | LLK |
9.88 ± 0.01 | S | Raymonda, 1972 | LLK |
9.89 | PE | Demeo and Yencha, 1970 | RDSH |
9.81 | PE | Dewar and Worley, 1969 | RDSH |
9.79 | PE | Al-Joboury and Turner, 1964 | RDSH |
9.88 ± 0.02 | PI | Watanabe, 1957 | RDSH |
11.0 ± 0.2 | EI | Hustrulid, Kusch, et al., 1938 | RDSH |
10.32 | PE | Kimura, Katsumata, et al., 1981 | Vertical value; LLK |
10.3 ± 0.1 | PE | Bieri, Burger, et al., 1977 | Vertical value; LLK |
10.3 | PE | Bruckmann and Klessinger, 1973 | Vertical value; LLK |
Appearance energy determinations
Ion | AE (eV) | Other Products | Method | Reference | Comment |
---|---|---|---|---|---|
C3H5+ | 13.20 ± 0.08 | C3H7 | EI | Rabbih, Selim, et al., 1981 | LLK |
C3H6+ | 12.00 ± 0.07 | C3H6 | EI | Rabbih, Selim, et al., 1981 | LLK |
C3H6+ | 11.23 ± 0.04 | C3H6 | PI | Sergeev, Akopyan, et al., 1973 | LLK |
C3H7+ | 13.50 ± 0.08 | C3H5 | EI | Rabbih, Selim, et al., 1981 | LLK |
C3H7+ | 11.49 ± 0.03 | C3H5 | PI | Sergeev, Akopyan, et al., 1973 | LLK |
C4H7+ | 11.21 ± 0.04 | C2H5 | PI | Sergeev, Akopyan, et al., 1973 | LLK |
C4H8+ | 11.15 ± 0.03 | C2H4 | EI | Rabbih, Selim, et al., 1981 | LLK |
C4H8+ | 11.45 | C2H4 | EI | Puttemans, 1974 | LLK |
C4H8+ | 11.08 ± 0.01 | C2H4 | PI | Sergeev, Akopyan, et al., 1973 | LLK |
C5H9+ | 9.88 | CH3 | EI | Lossing and Traeger, 1975, 2 | LLK |
C5H9+ | ≤11.06 | CH3 | EI | Lossing and Traeger, 1975 | LLK |
C5H9+ | 11.15 | CH3 | EI | Puttemans, 1974 | LLK |
C5H9+ | 11.07 ± 0.04 | CH3 | PI | Sergeev, Akopyan, et al., 1973 | LLK |
C6H11+ | 11.32 ± 0.05 | H | PI | Sergeev, Akopyan, et al., 1973 | LLK |
C6H11+ | 11.66 | H | EI | Pottie, Harrison, et al., 1961 | RDSH |
De-protonation reactions
C6H11- + =
By formula: C6H11- + H+ = C6H12
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1750. ± 8.4 | kJ/mol | Bran | Peerboom, Rademaker, et al., 1992 | gas phase; B |
ΔrH° | 1702.1 ± 3.8 | kJ/mol | G+TS | Bohme, Lee-Ruff, et al., 1972 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1713. ± 9.2 | kJ/mol | H-TS | Peerboom, Rademaker, et al., 1992 | gas phase; B |
ΔrG° | >1665.2 | kJ/mol | IMRB | Bohme, Lee-Ruff, et al., 1972 | gas phase; B |
Ion clustering 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: Michael M. Meot-Ner (Mautner) and Sharon G. Lias
Note: Please consider using the reaction search for this species. This page allows searching of all reactions involving this species. Searches may be limited to ion clustering reactions. A general reaction search form is also available.
Clustering reactions
By formula: C3H9Si+ + C6H12 = (C3H9Si+ • C6H12)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 159. | kJ/mol | PHPMS | Li and Stone, 1989 | gas phase; condensation |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 201. | J/mol*K | PHPMS | Li and Stone, 1989 | gas phase; condensation |
By formula: C6H6+ + C6H12 = (C6H6+ • C6H12)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 46.9 | kJ/mol | PHPMS | Meot-Ner (Mautner), Hamlet, et al., 1978 | gas phase; Entropy change calculated or estimated |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 110. | J/mol*K | N/A | Meot-Ner (Mautner), Hamlet, et al., 1978 | gas phase; Entropy change calculated or estimated |
Free energy of reaction
ΔrG° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
13. | 295. | PHPMS | Meot-Ner (Mautner), Hamlet, et al., 1978 | gas phase; Entropy change calculated or estimated |
By formula: H4N+ + C6H12 = (H4N+ • C6H12)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 40. | kJ/mol | PHPMS | Deakyne and Meot-Ner (Mautner), 1985 | gas phase; Entropy change calculated or estimated, DG<, ΔrH< |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 84. | J/mol*K | N/A | Deakyne and Meot-Ner (Mautner), 1985 | gas phase; Entropy change calculated or estimated, DG<, ΔrH< |
Free energy of reaction
ΔrG° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
12. | 317. | PHPMS | Deakyne and Meot-Ner (Mautner), 1985 | gas phase; Entropy change calculated or estimated, DG<, ΔrH< |
By formula: Li+ + C6H12 = (Li+ • C6H12)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 100. | kJ/mol | ICR | Staley and Beauchamp, 1975 | gas phase; switching reaction(Li+)H2O, from graph; Dzidic and Kebarle, 1970 extrapolated |
IR Spectrum
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Data compiled by: Coblentz Society, Inc.
- GAS (25 mmHg, N2 ADDED, TOTAL PRESSURE 600 mmHg); PERKIN-ELMER 180; DIGITIZED BY NIST FROM HARD COPY (FROM TWO SEGMENTS); 2 cm-1 resolution
- LIQUID (NEAT); DOW KBr FOREPRISM-GRATING; DIGITIZED BY COBLENTZ SOCIETY (BATCH I) FROM HARD COPY; 2 cm-1 resolution
- SOLUTION (10% CCl4 FOR 3800-1350, AND 10% CS2 FOR 1350-400 CM-1); DOW KBr FOREPRISM-GRATING; DIGITIZED BY COBLENTZ SOCIETY (BATCH I) FROM HARD COPY; 2 cm-1 resolution
Data compiled by: NIST Mass Spectrometry Data Center, William E. Wallace, director
Mass spectrum (electron ionization)
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, Gas phase ion energetics data, Ion clustering data, IR Spectrum, UV/Visible spectrum, Vibrational and/or electronic energy levels, 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: NIST Mass Spectrometry Data Center, William E. Wallace, director
Spectrum
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Additional Data
View image of digitized spectrum (can be printed in landscape orientation).
Due to licensing restrictions, this spectrum cannot be downloaded.
Owner | NIST Mass Spectrometry Data Center Collection (C) 2014 copyright by the U.S. Secretary of Commerce on behalf of the United States of America. All rights reserved. |
---|---|
Origin | NIST Mass Spectrometry Data Center, 1998. |
NIST MS number | 291493 |
UV/Visible spectrum
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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: Victor Talrose, Eugeny B. Stern, Antonina A. Goncharova, Natalia A. Messineva, Natalia V. Trusova, Margarita V. Efimkina
Spectrum
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Additional Data
View image of digitized spectrum (can be printed in landscape orientation).
View spectrum image in SVG format.
Download spectrum in JCAMP-DX format.
Source | Pickett, Muntz, et al., 1951 |
---|---|
Owner | INEP CP RAS, NIST OSRD Collection (C) 2007 copyright by the U.S. Secretary of Commerce on behalf of the United States of America. All rights reserved. |
Origin | INSTITUTE OF ENERGY PROBLEMS OF CHEMICAL PHYSICS, RAS |
Source reference | RAS UV No. 193 |
Instrument | Hilger prism spectrograph |
Melting point | 6.6 |
Boiling point | 80.7 |
Vibrational and/or electronic energy levels
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, Gas phase ion energetics data, Ion clustering data, IR Spectrum, Mass spectrum (electron ionization), UV/Visible spectrum, 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, Phase change data, Reaction thermochemistry data, Henry's Law data, Gas phase ion energetics data, Ion clustering data, IR Spectrum, Mass spectrum (electron ionization), UV/Visible spectrum, 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,
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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,
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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,
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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,
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Brickwedde F.G., 1946
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Equilibrium constants of some reactions involved in the production of 1,3-butadiene,
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Kilpatrick J.E., 1947
Kilpatrick J.E.,
Heats, equilibrium constants, and free energies of formation of the alkylcyclopentanes and alkylcyclohexanes,
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Lippincott E.R., 1966
Lippincott E.R.,
Enthalpy, free energy, entropy, and heat capacity of cyclohexane and acetaldehyde,
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Spitzer R., 1946
Spitzer R.,
The heat capacity of gaseous cyclopentane, cyclohexane and methylcyclohexane,
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Montgomery J.B., 1942
Montgomery J.B.,
The heat capacity of organic vapors. IV. Benzene, fluorobenzene, toluene, cyclohexane, methylcyclohexane and cyclohexene,
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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,
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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,
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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,
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Voss and Sloan, 1989
Voss, S.F.; Sloan, E.D.,
Thermal conductivity and heat capacity of synthetic fuel components,
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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,
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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,
J. Chem. Thermodynam., 1988, 20, 1307-1314. [all data]
Kalali, Kohler, et al., 1987
Kalali, H.; Kohler, F.; Svejda, P.,
Excess properties of the mixture bis(2-dichlorethyl)ether (chlorex) + 2,2,4-trimethylpentane (isooctane),
Monatsh. Chem., 1987, 118, 1-18. [all data]
Jimenez, Romani, et al., 1986
Jimenez, E.; Romani, L.; Paz Andrade, M.I.; Roux-Desgranges, G.; Grolier, J.-P.E.,
Molar excess heat capacities and volumes for mixtures of alkanoates with cyclohexane at 25°C,
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Ortega, 1986
Ortega, J.,
Excess molar heat capacities of the binary mixtures of cyclohexane with isomers of hexanol at 298.15 K,
Rev. Latinoam. Ing. Quim. Quim. Apl., 1986, 16, 307-315. [all data]
Nkinamubanzi, Charlet, et al., 1985
Nkinamubanzi, P.; Charlet, G.; Delmas, G.,
Excess enthalpies, excess heat capacities and excess volumes of tetraalkoxysilanes with cyclohexane and carbon tetrachloride,
Fluid Phase Equilibria, 1985, 20, 57-73. [all data]
Tanaka, Nakamichi, et al., 1985
Tanaka, R.; Nakamichi, T.; Murakami, S.,
Molar excess heat capacities and volumes for mixtures of benzomitrile with cyclohexane between 10 and 45°C,
J. Solution Chem., 1985, 14(11), 795-803. [all data]
Siddiqi, Svejda, et al., 1983
Siddiqi, M.A.; Svejda, P.; Kohler, F.,
A generalized van der Waals equation of state II. Excess heat capacities of mixtures containing cycloalkanes (C5,C6), methylcycloalkanes (C5,C6) and n-decane,
Ber. Bunsenges. Phys. Chem., 1983, 87, 1176-1181. [all data]
Grolier, Inglese, et al., 1982
Grolier, J.-P.E.; Inglese, A.; Wilhelm, E.,
Excess volumes and excess heat capacities of tetrachloroethene + cyclohexane, + methylcyclohexane, + benzene, and + toluene at 298.15 K,
J. Chem. Thermodynam., 1982, 14, 523-529. [all data]
Tanaka, 1982
Tanaka, R.,
Determination of excess heat capacities of (benzene + tetrachloromethane and + cyclohexane) between 293.15 and 303.15 K by use of a Picker flow calorimeter,
J. Chem. Thermodynam., 1982, 14, 259-268. [all data]
Fortier, D'Arcy, et al., 1979
Fortier, J.-L.; D'Arcy, P.J.; Benson, G.C.,
Heat capacities of binary cycloalkane mixtures at 298.15 K,
Thermochim. Acta, 1979, 28, 37-43. [all data]
Vesely, Zabransky, et al., 1979
Vesely, F.; Zabransky, M.; Svoboda, V.; Pick, J.,
The use of mixing calorimeter for measuring heat capacities of liquids,
Coll. Czech. Chem. Commun., 1979, 44, 3529-3532. [all data]
Wilhelm, Grolier, et al., 1979
Wilhelm, E.; Grolier, G.-P.E.; Karbalai Ghassemi, M.H.,
Molar heat capacity of binary liquid mixtures: 1,2-dichloroethane + cyclohexane and 1,2-dichloroethane + methylcyclohexane,
Thermochim. Acta, 1979, 28, 59-69. [all data]
Grolier, Wilhelm, et al., 1978
Grolier, J.-P.E.; Wilhelm, E.; Hamedi, M.H.,
Molar heat capacities and isothermal compressibility of binary liquid mixtures: carbon tetrachloride + benzene, carbon tetrachloride + cyclohexane and benzene + cyclohexane,
Ber. Bunsenges. Phys. Chem., 1978, 82, 1282-1290. [all data]
Safir, 1978
Safir, L.I.,
Experimental determination of the isobaric heat capacity of cyclohexane at atmospheric pressure,
Izv. Vyssh. Uchebn. Zaved. Neft. Gaz 21, 1978, (12), 81-82. [all data]
Vesely, Svoboda, et al., 1977
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Notes
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, Gas phase ion energetics data, Ion clustering data, IR Spectrum, Mass spectrum (electron ionization), UV/Visible spectrum, Vibrational and/or electronic energy levels, References
- Symbols used in this document:
AE Appearance energy Cp,gas Constant pressure heat capacity of gas Cp,liquid Constant pressure heat capacity of liquid IE (evaluated) Recommended ionization energy Pc Critical pressure S°gas Entropy of gas at standard conditions S°liquid Entropy of liquid at standard conditions T Temperature Tboil Boiling point Tc Critical temperature Tfus Fusion (melting) point Ttriple Triple point temperature Vc Critical volume d(ln(kH))/d(1/T) Temperature dependence parameter for Henry's Law constant k°H Henry's Law constant at 298.15K ΔHtrs Enthalpy of phase transition ΔStrs Entropy of phase transition 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 ΔrG° Free energy of reaction at standard conditions ΔrH° Enthalpy of reaction at standard conditions ΔrS° Entropy 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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