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.
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Phase change data
Go To: Top, Reaction thermochemistry data, Gas phase ion energetics data, References, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data compiled as indicated in comments:
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)
View plot Requires a JavaScript / HTML 5 canvas capable browser.
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)
View plot Requires a JavaScript / HTML 5 canvas capable browser.
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, Phase change data, Gas phase ion energetics data, References, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data compiled as indicated in comments:
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
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 |
Gas phase ion energetics data
Go To: Top, Phase change data, Reaction thermochemistry data, References, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data evaluated as indicated in comments:
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 |
References
Go To: Top, Phase change data, Reaction thermochemistry data, Gas phase ion energetics data, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Daubert, 1996
Daubert, T.E.,
Vapor-Liquid Critical Properties of Elements and Compounds. 5. Branched Alkanes and Cycloalkanes,
J. Chem. Eng. Data, 1996, 41, 365-372. [all data]
Young, 1972
Young, C.L.,
Gas-liquid critical properties of the cycloalkanes and their mixtures,
Aust. J. Chem., 1972, 25, 1625-30. [all data]
Teja and Anselme, 1990
Teja, A.S.; Anselme, M.J.,
The critical properties of thermally stable and unstable fluids. II. 1986 results,
AIChE Symp. Ser., 1990, 86, 279, 122-7. [all data]
Simon, 1957
Simon, M.,
Methods and Apparatus Used at the Bureau of Physicochemical Standards XV. Critical Constants and Straight-Line Diameters of Ten Hydrocarbons,
Bull. Soc. Chim. Belg., 1957, 66, 375-81. [all data]
Young, 1910
Young, S.,
The Internal Heat of Vaporization constants of thirty pure substances,
Sci. Proc. R. Dublin Soc., 1910, 12, 374. [all data]
Young and Fortey, 1899
Young, S.; Fortey, E.C.,
The Vapour Pressures, Specific Volumes and Critical Constants of Hexamethylene.,
J. Chem. Soc., Trans., 1899, 75, 873. [all data]
Majer and Svoboda, 1985
Majer, V.; Svoboda, V.,
Enthalpies of Vaporization of Organic Compounds: A Critical Review and Data Compilation, Blackwell Scientific Publications, Oxford, 1985, 300. [all data]
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]
Gierycz, Kosowski, et al., 2009
Gierycz, Pawel; Kosowski, Andrzej; Swietlik, Ryszard,
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols,
J. Chem. Eng. Data, 2009, 54, 11, 2996-3001, https://doi.org/10.1021/je900050z
. [all data]
Lubomska, Banas, et al., 2002
Lubomska, Monika; Banas, Agnieszka; Malanowski, Stanislaw K.,
Vapor-Liquid Equilibrium in Binary Systems Formed by Allyl Alcohol with Benzene and with Cyclohexane,
J. Chem. Eng. Data, 2002, 47, 6, 1466-1471, https://doi.org/10.1021/je025540l
. [all data]
Diogo, Santos, et al., 1995
Diogo, Hermínio P.; Santos, Rui C.; Nunes, Paulo M.; Minas da Piedade, Manuel E.,
Ebulliometric apparatus for the measurement of enthalpies of vaporization,
Thermochimica Acta, 1995, 249, 113-120, https://doi.org/10.1016/0040-6031(95)90678-9
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Lee and Holder, 1993
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Notes
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- Symbols used in this document:
AE Appearance energy IE (evaluated) Recommended ionization energy Pc Critical pressure T Temperature Tboil Boiling point Tc Critical temperature Tfus Fusion (melting) point Ttriple Triple point temperature Vc Critical volume ΔHtrs Enthalpy of phase transition ΔStrs Entropy of phase transition 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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