Naphthalene
- Formula: C10H8
- Molecular weight: 128.1705
- IUPAC Standard InChIKey: UFWIBTONFRDIAS-UHFFFAOYSA-N
- CAS Registry Number: 91-20-3
- 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: Albocarbon; Dezodorator; Moth flakes; Naphthalin; Naphthaline; Naphthene; Tar camphor; White tar; Camphor tar; Moth balls; Naftalen; NCI-C52904; Mighty 150; Mighty RD1; Rcra waste number U165; UN 1334; UN 2304; NSC 37565
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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, 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 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 | 150. ± 10. | kJ/mol | AVG | N/A | Average of 7 values; Individual data points |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
36.18 | 50. | Thermodynamics Research Center, 1997 | p=1 bar. Selected values of S(T) and Cp(T) agree with those calculated by statistical thermodynamics method [ Dorofeeva O.V., 1986, Dorofeeva O.V., 1988] within 1.2 J/mol*K. Discrepancies with other calculations [ Barrow G.M., 1951, McClellan A.L., 1955, 79CHE/KUD, Lielmezs J., 1981] reach 2-3 J/mol*K.; GT |
47.50 | 100. | ||
63.89 | 150. | ||
84.99 | 200. | ||
120.52 | 273.15 | ||
133.02 | 298.15 | ||
133.94 | 300. | ||
181.16 | 400. | ||
220.70 | 500. | ||
252.37 | 600. | ||
277.77 | 700. | ||
298.43 | 800. | ||
315.50 | 900. | ||
329.77 | 1000. | ||
341.8 | 1100. | ||
352.0 | 1200. | ||
360.8 | 1300. | ||
368.2 | 1400. | ||
374.7 | 1500. |
Constant pressure heat capacity of gas
Cp,gas (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
201.6 ± 2.0 | 451.0 | Barrow G.M., 1951 | GT |
226.7 ± 2.3 | 522.7 |
Condensed phase thermochemistry data
Go To: Top, Gas phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law 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 as indicated in comments:
DH - Eugene S. Domalski and Elizabeth D. Hearing
DRB - Donald R. Burgess, Jr.
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
S°liquid | 217.59 | J/mol*K | N/A | Chirico, Knipmeyer, et al., 1993 | DH |
Quantity | Value | Units | Method | Reference | Comment |
ΔfH°solid | 77. ± 10. | kJ/mol | AVG | N/A | Average of 7 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°solid | -5160. ± 20. | kJ/mol | AVG | N/A | Average of 18 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
S°solid,1 bar | 167.40 | J/mol*K | N/A | McCullough, Finke, et al., 1957 | DH |
S°solid,1 bar | 162.84 | J/mol*K | N/A | Southard and Brickwedde, 1933 | DH |
S°solid,1 bar | 166.86 | J/mol*K | N/A | Pearce and Tanner, 1934 | Extrapolation below 90 K, 58.32 J/mol*K.; DH |
S°solid,1 bar | 166.9 | J/mol*K | N/A | Huffman, Parks, et al., 1930 | Extrapolation below 90 K, 53.09 J/mol*K.; DH |
Constant pressure heat capacity of liquid
Cp,liquid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
196.06 | 298.15 | Chirico, Knipmeyer, et al., 1993 | T = 260 to 700 K.; DH |
Constant pressure heat capacity of solid
Cp,solid (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
213. | 330. | David, 1964 | T = 298 to 353 K. Mean value. T = uncertain.; DH |
188.4 | 342. | Rastogi and Bassi, 1964 | T = 342, 384 K.; DH |
165.69 | 298.15 | McCullough, Finke, et al., 1957 | T = 10 to 370 K.; DH |
156.1 | 298.15 | Ueberreiter and Orthmann, 1950 | T = 293 to 368 K. Equation only.; DH |
195.8 | 298.1 | Eibert, 1944 | T = 30 to 200°C, equations only in t°C. Cp(c) = 0.365 cal/g*K (30 to 80°C); Cp(liq) = 0.329 + 0.000824t cal/g*K (80 to 200°C).; DH |
161.5 | 298.1 | Schmidt, 1941 | T = 22 to 200°C, equations only, in t°C. Cp(c) = 0.2595 + 0.001672t cal/g*K (22 to 80°C); Cp(liq) = 0.3360 + 0.0008180t cal/g*K (80 to 200°C).; DH |
168.11 | 301.58 | Hicks, 1938 | T = 58 to 304 K. Value is unsmoothed experimental datum.; DH |
168.07 | 297.6 | Pearce and Tanner, 1934 | T = 94 to 298 K. Value is unsmoothed experimental datum.; DH |
165.48 | 294.68 | Southard and Brickwedde, 1933 | T = 15 to 295 K. Value is unsmoothed experimental datum.; DH |
169.0 | 303. | Spaght, Thomas, et al., 1932 | T = 30 to 190°C.; DH |
163.6 | 295.1 | Huffman, Parks, et al., 1930 | T = 91 to 295 K.; DH |
159.4 | 298. | Andrews, Lynn, et al., 1926 | T = 12 to 300°C.; DH |
Phase change data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Reaction thermochemistry data, Henry's Law 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 as indicated in comments:
BS - Robert L. Brown and Stephen E. Stein
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, Chris Muzny director
AC - William E. Acree, Jr., James S. Chickos
DH - Eugene S. Domalski and Elizabeth D. Hearing
DRB - Donald R. Burgess, Jr.
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 490. ± 5. | K | AVG | N/A | Average of 10 out of 11 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 353.2 ± 0.7 | K | AVG | N/A | Average of 55 out of 57 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 353.39 ± 0.09 | K | AVG | N/A | Average of 6 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 748. ± 6. | K | AVG | N/A | Average of 13 out of 14 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 41. ± 1. | bar | AVG | N/A | Average of 10 out of 11 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Vc | 0.407 | l/mol | N/A | Tsonopoulos and Ambrose, 1995 | |
Vc | 0.409 | l/mol | N/A | Cheng, 1963 | Uncertainty assigned by TRC = 0.06 l/mol; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 2.46 ± 0.05 | mol/l | N/A | Tsonopoulos and Ambrose, 1995 | |
ρc | 2.497 | mol/l | N/A | Chirico, Knipmeyer, et al., 1993, 2 | Uncertainty assigned by TRC = 0.078 mol/l; TRC |
ρc | 2.450 | mol/l | N/A | Schroeer, 1941 | Uncertainty assigned by TRC = 0.04 mol/l; TRC |
ρc | 2.456 | mol/l | N/A | Zhuravlev, 1937 | Uncertainty assigned by TRC = 0.04 mol/l; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 54.6 | kJ/mol | CGC | Zhao, Unhannanant, et al., 2008 | AC |
ΔvapH° | 60.3 ± 1.1 | kJ/mol | GC | Haftka, Parsons, et al., 2006 | Based on data from 333. to 403. K.; AC |
ΔvapH° | 53.4 | kJ/mol | CGC | Chickos, Hesse, et al., 1998 | AC |
ΔvapH° | 56.6 | kJ/mol | CGC | Chickos, Hosseini, et al., 1995 | Based on data from 403. to 453. K.; AC |
Quantity | Value | Units | Method | Reference | Comment |
ΔsubH° | 71. ± 5. | kJ/mol | AVG | N/A | Average of 17 values; Individual data points |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
70.850 | 323. | N/A | Torres-Gomez, Barreiro-Rodriguez, et al., 1988 | DH |
56.1 | 398. | GC | Lei, Chankalal, et al., 2002 | Based on data from 323. to 473. K.; AC |
47.6 ± 1.8 | 491. to 747. | DSC | Boller and Wiedemann, 1998 | AC |
45.4 | 475. | DSC | Back, Grzyll, et al., 1996 | Based on data from 460. to 647. K.; AC |
48.7 ± 0.3 | 400. | EB | Chirico, Knipmeyer, et al., 1993 | AC |
46.4 | 440. | EB | Chirico, Knipmeyer, et al., 1993 | AC |
44.0 | 480. | EB | Chirico, Knipmeyer, et al., 1993 | AC |
41.5 | 520. | EB | Chirico, Knipmeyer, et al., 1993 | AC |
44.4 | 528. | N/A | Lee and Holder, 1993 | Based on data from 513. to 613. K.; AC |
47.9 | 423. | EB | Ambrose, Ewing, et al., 1990 | Based on data from 418. to 613. K.; AC |
50.6 | 367. | A | Stephenson and Malanowski, 1987 | Based on data from 352. to 500. K.; AC |
44.8 | 506. | A | Stephenson and Malanowski, 1987 | Based on data from 491. to 565. K.; AC |
43.2 | 578. | A | Stephenson and Malanowski, 1987 | Based on data from 563. to 663. K.; AC |
43.3 | 676. | A | Stephenson and Malanowski, 1987 | Based on data from 661. to 750. K.; AC |
50.3 ± 0.2 | 370. | N/A | de Kruif, Kuipers, et al., 1981 | Based on data from 353. to 388. K.; AC |
44.7 | 466. | N/A | Wilson, Johnston, et al., 1981 | Based on data from 441. to 727. K.; AC |
50.7 | 369. | N/A | Fowler, Trump, et al., 1968 | Based on data from 354. to 453. K.; AC |
49.0 | 414. | N/A | Camin and Rossini, 1955 | Based on data from 399. to 491. K.; AC |
46.4 | 441. | C | Barrow and McClellan, 1951 | AC |
48.3 | 379. | I | Cramer, 1943 | AC |
47.2 | 423. | I | Mortimer and Murphy, 1923 | Based on data from 373. to 473. K.; AC |
47.7 | 427. | I | NELSON and SENSEMAN, 1922 | Based on data from 360. to 494. K.; AC |
Entropy of vaporization
ΔvapS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
219.3 | 323. | Torres-Gomez, Barreiro-Rodriguez, et al., 1988 | 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 |
---|---|---|---|---|---|
353.48 to 452.30 | 4.27117 | 1831.571 | -61.329 | Fowler, Trump, et al., 1968 | Coefficents calculated by NIST from author's data. |
399.47 to 491.79 | 3.97067 | 1606.529 | -85.923 | Camin and Rossini, 1955 |
Enthalpy of sublimation
ΔsubH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
72.320 | 298.15 | N/A | Torres-Gomez, Barreiro-Rodriguez, et al., 1988 | DH |
72.8 | 327. | GS | Grayson and Fosbraey, 2006 | Based on data from 302. to 352. K.; AC |
64. ± 0.5 | 281. to 290. | LE | McEachern and Sandoval, 2001 | AC |
88.0 ± 2.5 | 267. to 303. | ME | Boller and Wiedemann, 1998 | AC |
71.7 | 333. | GS | Nass, Lenoir, et al., 1995 | Based on data from 313. to 353. K.; AC |
73.7 ± 1.0 | 258. | GS | Wania, Shiu, et al., 1994 | Based on data from 243. to 273. K.; AC |
78. ± 1. | 337. to 352. | GC | Khudyakov, 1988 | AC |
71. ± 4. | 323. | DSC | Torres-Gomez, Barreiro-Rodriguez, et al., 1988 | AC |
73.4 | 315. | GS | SATO, INOMATA, et al., 1986 | Based on data from 299. to 331. K.; AC |
72.3 ± 0.8 | 293. to 331. | QR | Glukhova, Arkhangelova, et al., 1985 | AC |
69.9 | 333. to 393. | GS | Matsubara and Kuwamoto, 1985 | AC |
75.8 ± 1.1 | 303. | GS | Sonnefeld, Zoller, et al., 1983 | Based on data from 283. to 323. K.; AC |
72.8 ± 0.3 | 271. to 285. | ME | Colomina, Jimenez, et al., 1982 | AC |
72.5 ± 0.1 | 274. to 353. | DM | de Kruif, Kuipers, et al., 1981 | AC |
72.6 ± 0.6 | 253. to 273. | TE | Kruif, 1980 | AC |
76.0 ± 2.0 | 328. to 398. | DSC | Murray, Cavell, et al., 1980 | AC |
71.3 | 293. | GS | Macknick and Prausnitz, 1979 | Based on data from 280. to 305. K.; AC |
74.8 ± 0.4 | 253. to 273. | TE | De Kruif and Van Ginkel, 1977 | AC |
73.9 ± 0.2 | 253. to 273. | ME | De Kruif and Van Ginkel, 1977 | AC |
72.5 ± 0.3 | 263. to 343. | DM | Ambrose, Lawrenson, et al., 1975 | AC |
67.8 ± 3.5 | 280. | HSA | Chickos, 1975 | AC |
74.4 ± 1.7 | 303. to 329. | TSGC | McEachern, Sandoval, et al., 1975 | AC |
72.7 ± 1.7 | 283. | V | Radchenko and Kitaigorodskii, 1974 | ALS |
72.7 | 283. to 323. | ME | Radchenko, 1971 | AC |
66.53 ± 0.84 | 283. | V | Karyakin, Rabinovich, et al., 1968 | ALS |
72.7 ± 0.3 | 230. to 260. | KG | Miller, 1963 | See also Cox and Pilcher, 1970.; AC |
66.3 ± 2.3 | 354.7 | V | Aihara, 1959 | crystal phase; ALS |
66.3 | 276. to 283. | V | Aihara, 1959, 2 | AC |
69.2 | 268. | N/A | Hoyer and Peperle, 1958 | Based on data from 253. to 283. K.; AC |
65.8 | 293. | Effusion | Sklyarenko, Markin, et al., 1958 | Based on data from 283. to 303. K.; AC |
72.1 | 292. | N/A | Sherwood and Bryant, 1957 | Based on data from 273. to 311. K.; AC |
72.4 | 279. to 294. | N/A | Bradley and Cleasby, 1953 | See also Jones, 1960 and Sears and Hopke, 1954.; AC |
72.383 | 279.7 | V | Bradley and Cleasby, 1953, 2 | ALS |
65.7 | 297. | Effusion | Zibberman-Granovskaya, 1940 | Based on data from 288. to 306. K.; AC |
76.6 | 237. to 276. | N/A | Andrews, 1925 | AC |
82.0 | 293. | ME | Swan and Mack, 1925 | Based on data from 283. to 303. K.; AC |
Entropy of sublimation
ΔsubS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
242.6 | 298.15 | Torres-Gomez, Barreiro-Rodriguez, et al., 1988 | DH |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
18.811 | 353.44 | N/A | Mastrangelo, 1957 | DH |
18.226 | 353.43 | N/A | McCullough, Finke, et al., 1957 | DH |
19.200 | 353.0 | N/A | Spaght, Thomas, et al., 1932 | DH |
19.1 | 353.5 | DSC | Sharma, Gupta, et al., 2008 | AC |
16.44 | 353.8 | DSC | Hafsaoui and Mahmoud, 2007 | AC |
19.55 | 354.7 | DSC | Khimeche and Dahmani, 2006 | AC |
19.55 | 354.7 | DSC | Khimeche and Dahmani, 2006, 2 | AC |
19.0 | 353.4 | AC | Chirico, Knipmeyer, et al., 2002 | Based on data from 5. to 440. K.; AC |
19.1 | 353.4 | N/A | Acree, 1991 | AC |
19.020 | 354.1 | N/A | Syunyaev, Tumanyan, et al., 1984 | Relative error in determination ± 5%.; DH |
19.100 | 353.5 | N/A | Rastogi and Bassi, 1964 | DH |
18.785 | 353. | N/A | Ueberreiter and Orthmann, 1950 | DH |
18.790 | 353.4 | N/A | Eibert, 1944 | DH |
19.040 | 353.4 | N/A | Schmidt, 1941 | DH |
19.000 | 353.1 | N/A | Andrews, Lynn, et al., 1926 | DH |
19.250 | 353. | N/A | David, 1964 | Temperature not measured.; DH |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
51.57 | 353.43 | McCullough, Finke, et al., 1957 | DH |
54.4 | 353.0 | Spaght, Thomas, et al., 1932 | DH |
53.7 | 354.1 | Syunyaev, Tumanyan, et al., 1984 | Relative; DH |
54.0 | 353.5 | Rastogi and Bassi, 1964 | DH |
53.2 | 353. | Ueberreiter and Orthmann, 1950 | DH |
53.2 | 353.4 | Eibert, 1944 | DH |
53.9 | 353.4 | Schmidt, 1941 | DH |
53.8 | 353.1 | Andrews, Lynn, et al., 1926 | DH |
55. | 353. | David, 1964 | Temperature; DH |
Enthalpy of phase transition
ΔHtrs (kJ/mol) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
19.046 | 353.376 | crystaline, I | liquid | Andon and Connett, 1980 | DH |
19.000 | 353.8 | crystaline, I | liquid | Radomska and Radomski, 1980 | DH |
Entropy of phase transition
ΔStrs (J/mol*K) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
53.90 | 353.376 | crystaline, I | liquid | Andon and Connett, 1980 | DH |
53.70 | 353.8 | crystaline, I | liquid | Radomska and Radomski, 1980 | DH |
Reaction thermochemistry data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Henry's Law 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 as indicated in comments:
B - John E. Bartmess
M - Michael M. Meot-Ner (Mautner) and Sharon G. Lias
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
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
C10H7- + =
By formula: C10H7- + H+ = C10H8
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1649. ± 5.0 | kJ/mol | Bran | Reed and Kass, 2000 | gas phase; B |
ΔrH° | 1649. ± 5.0 | kJ/mol | TDEq | Meot-ner, Liebman, et al., 1988 | gas phase; anchored to 88MEO scale, not the "87 acidity scale". The Kiefer, Zhang, et al., 1997 BDE is for ortho.; B |
ΔrH° | 1648. ± 21. | kJ/mol | CIDC | Lardin, Squires, et al., 2001 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1613. ± 5.4 | kJ/mol | H-TS | Reed and Kass, 2000 | gas phase; B |
ΔrG° | 1606. ± 5.0 | kJ/mol | TDEq | Meot-ner, Liebman, et al., 1988 | gas phase; anchored to 88MEO scale, not the "87 acidity scale". The Kiefer, Zhang, et al., 1997 BDE is for ortho.; B |
ΔrG° | 1613. ± 21. | kJ/mol | H-TS | Lardin, Squires, et al., 2001 | gas phase; B |
By formula: C6H7N+ + C10H8 = (C6H7N+ • C10H8)
Bond type: Charge transfer bond (positive ion)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 64.4 | kJ/mol | PHPMS | El-Shall and Meot-Ner (Mautner), 1987 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 110. | J/mol*K | N/A | El-Shall and Meot-Ner (Mautner), 1987 | gas phase; Entropy change calculated or estimated; M |
Free energy of reaction
ΔrG° (kJ/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
31. | 324. | PHPMS | El-Shall and Meot-Ner (Mautner), 1987 | gas phase; Entropy change calculated or estimated; M |
By formula: C12H8+ + C10H8 = (C12H8+ • C10H8)
Bond type: Charge transfer bond (positive ion)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 52.7 | kJ/mol | PHPMS | Meot-Ner (Mautner), 1980 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 120. | J/mol*K | N/A | Meot-Ner (Mautner), 1980 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 21. | kJ/mol | PHPMS | Meot-Ner (Mautner), 1980 | gas phase; Entropy change calculated or estimated; M |
By formula: C12H9+ + C10H8 = (C12H9+ • C10H8)
Bond type: Charge transfer bond (positive ion)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 58.2 | kJ/mol | PHPMS | Meot-Ner (Mautner), 1980 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 120. | J/mol*K | N/A | Meot-Ner (Mautner), 1980 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 27. | kJ/mol | PHPMS | Meot-Ner (Mautner), 1980 | gas phase; Entropy change calculated or estimated; M |
By formula: 2H2 + C10H8 = C10H12
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -125. | kJ/mol | Eqk | Frye and Weitkamp, 1969 | gas phase; ALS |
ΔrH° | -120.5 ± 5.0 | kJ/mol | Eqk | Wilson, Caflisch, et al., 1958 | gas phase; Reanalyzed by Cox and Pilcher, 1970, 2, Original value = -133.9 ± 5.0 kJ/mol; At 400 K; ALS |
By formula: C10H8 = C10H8
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -248.5 ± 8.0 | kJ/mol | Eqk | Dreeskamp, Kapahnke, et al., 1988 | liquid phase; solvent: Heptane; Isomerization; ALS |
ΔrH° | -249.2 ± 8.0 | kJ/mol | Ciso | Grimme and Heinze, 1978 | liquid phase; solvent: Heptane; ALS |
By formula: C10H8+ + C10H8 = (C10H8+ • C10H8)
Bond type: Charge transfer bond (positive ion)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 74.5 | kJ/mol | PHPMS | Meot-Ner (Mautner), 1980 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 120. | J/mol*K | PHPMS | Meot-Ner (Mautner), 1980 | gas phase; M |
C10H7- + =
By formula: C10H7- + H+ = C10H8
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 1655. ± 5.4 | kJ/mol | Bran | Reed and Kass, 2000 | gas phase; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 1619. ± 5.9 | kJ/mol | H-TS | Reed and Kass, 2000 | gas phase; B |
By formula: H4O4- + C10H8 + 2H2O = C10H12O4-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 219. ± 9.6 | kJ/mol | N/A | Le Barbu, Schiedt, et al., 2002 | gas phase; Affinity is difference in EAs of lesser solvated species; B |
By formula: H2O3- + C10H8 + H2O = C10H10O3-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 158. ± 9.6 | kJ/mol | N/A | Le Barbu, Schiedt, et al., 2002 | gas phase; Affinity is difference in EAs of lesser solvated species; B |
By formula: C10H9+ + C10H8 = (C10H9+ • C10H8)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 59.0 | kJ/mol | PHPMS | Meot-Ner (Mautner), 1980 | gas phase; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 130. | J/mol*K | PHPMS | Meot-Ner (Mautner), 1980 | gas phase; M |
+ = C10H8O2-
By formula: O2- + C10H8 = C10H8O2-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 92.5 ± 9.6 | kJ/mol | N/A | Le Barbu, Schiedt, et al., 2002 | gas phase; Affinity is difference in EAs of lesser solvated species; B |
+ = C10H8NO-
By formula: NO- + C10H8 = C10H8NO-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 60.7 ± 9.6 | kJ/mol | N/A | Le Barbu, Schiedt, et al., 2002 | gas phase; Affinity is difference in EAs of lesser solvated species; B |
By formula: C10H8NO- + 2C10H8 = C20H16NO-
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 99.6 ± 9.6 | kJ/mol | N/A | Le Barbu, Schiedt, et al., 2002 | gas phase; Affinity is difference in EAs of lesser solvated species; B |
By formula: 5H2 + C10H8 = C10H18
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -318. | kJ/mol | Eqk | Frye and Weitkamp, 1969 | gas phase; ALS |
Henry's Law data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry 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: 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 |
---|---|---|---|---|
0.80 | Q | N/A | missing citation give several references for the Henry's law constants but don't assign them to specific species. | |
2.0 | X | N/A | ||
2.1 | 3600. | X | N/A | |
2.4 | L | N/A | ||
2.1 | M | Mackay, Shiu, et al., 1979 | ||
2.1 | T | Mackay, Shiu, et al., 1979 | ||
2.4 | V | N/A | ||
1.9 | V | Bohon and Claussen, 1951 |
IR Spectrum
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, Mass spectrum (electron ionization), UV/Visible spectrum, References, Notes
Data compiled by: Coblentz Society, Inc.
- SOLUTION (10% CCl4 FOR 3800-1300, 11% CS2 FOR 1300-650, AND 10% CCl4 FOR 650-250); PERKIN-ELMER 521 (GRATING); 2 cm-1 resolution
- VAPOR (1.0 MICROLITER AT 245 C); NICOLET FTIR; DIGITIZED BY NIST FROM HARD COPY (FROM TWO SEGMENTS); 4 CM-1 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, IR Spectrum, 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: 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 | Japan AIST/NIMC Database- Spectrum MS-NW-1434 |
NIST MS number | 228342 |
UV/Visible spectrum
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, IR Spectrum, Mass spectrum (electron ionization), 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: 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 | Ferguson, Reeves, et al., 1957 |
---|---|
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. 1174 |
Instrument | Beckman DU |
Melting point | 80.2 |
Boiling point | 217.9 |
References
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, IR Spectrum, Mass spectrum (electron ionization), UV/Visible spectrum, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
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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 Cp,solid Constant pressure heat capacity of solid Pc Critical pressure S°liquid Entropy of liquid at standard conditions S°solid,1 bar Entropy of solid at standard conditions (1 bar) 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°solid Enthalpy of combustion of solid at standard conditions ΔfH°gas Enthalpy of formation of gas at standard conditions ΔfH°solid Enthalpy of formation of solid 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 ΔsubH° Enthalpy of sublimation at standard conditions ΔsubS Entropy 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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