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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Condensed phase thermochemistry data
Go To: Top, Phase change 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:
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, Condensed phase thermochemistry data, References, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data compiled 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)
View plot Requires a JavaScript / HTML 5 canvas capable browser.
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 |
References
Go To: Top, Condensed phase thermochemistry data, Phase change data, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Chirico, Knipmeyer, et al., 1993
Chirico, R.D.; Knipmeyer, S.E.; Nguyen, A.; Steele, W.V.,
The thermodynamic properties to the temperature 700 K of naphthalene and of 2,7-dimethylnaphthalene,
J. Chem. Thermodyn., 1993, 25, 1461-1494. [all data]
McCullough, Finke, et al., 1957
McCullough, J.P.; Finke, H.L.; Messerly, J.F.; Kincheloe, T.C.; Waddington, G.,
The low temperature thermodynamic properties of naphthalene, 1-methylnaphthalene, 2-methylnaphthalene, 1,2,3,4-tetrahydronaphthalene, trans-decahydronaphthalene and cis-decahydronaphthalene,
J. Phys. Chem., 1957, 61, 1105-1116. [all data]
Southard and Brickwedde, 1933
Southard, J.C.; Brickwedde, F.G.,
Low temperature specific heats. I. An improved calorimeter for use from 14 to 300 K. The heat capacity and entropy of naphthalene. J. Am. Chem. Soc., 1933, 4378-4384. [all data]
Pearce and Tanner, 1934
Pearce, J.N.; Tanner, W.B.,
The heat capacity and the free energy of formation of naphthalene,
Proc. Iowa Acad. Sci., 1934, 41, 123-126. [all data]
Huffman, Parks, et al., 1930
Huffman, H.M.; Parks, G.S.; Daniels, A.C.,
Thermal data on organic compounds. VII. The heat capacities, entropies and free energies of twelve aromatic hydrocarbons,
J. Am. Chem. Soc., 1930, 52, 1547-1558. [all data]
David, 1964
David, D.J.,
Determination of specific heat and heat of fusion by differential thermal analysis. Study of theory and operating parameters,
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Rastogi and Bassi, 1964
Rastogi, R.P.; Bassi, P.S.,
Mechanism of eutectic crystallization,
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Ueberreiter and Orthmann, 1950
Ueberreiter, K.; Orthmann, H.-J.,
Specifische Wärme, spezifisches Volumen, Temperatur- und Wärme-leittähigkeit einiger disubstituierter Benzole und polycyclischer Systeme,
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Eibert, 1944
Eibert, J.,
Thesis Washington University (St. Louis), 1944. [all data]
Schmidt, 1941
Schmidt, W.R.,
Thesis Washington University (St. Louis), 1941. [all data]
Hicks, 1938
Hicks, J.F.G., Jr.,
A low temperature calorimeter. The heat capacity and entropy of thallium from 14 to 300°K. Low temperature studies. No. 3,
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Spaght, Thomas, et al., 1932
Spaght, M.E.; Thomas, S.B.; Parks, G.S.,
Some heat capacity data on organic compounds obtained with a radiation calorimeter,
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Andrews, Lynn, et al., 1926
Andrews, D.H.; Lynn, G.; Johnston, J.,
The heat capacities and heat of crystallization of some isomeric aromatic compounds,
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Tsonopoulos and Ambrose, 1995
Tsonopoulos, C.; Ambrose, D.,
Vapor-Liquid Critical Properties of Elements and Compounds. 3. Aromatic Hydrocarbons,
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Cheng, 1963
Cheng, D.C.H.,
Critical temperatures and volumes of some binary systems,
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Chirico, Knipmeyer, et al., 1993, 2
Chirico, R.D.; Knipmeyer, S.E.; Nguyen, A.; Steele, W.V.,
The thermodynamic properties to the temperature 700 K of naphthalene and of 2,7-dimethylnaphthalene,
J. Chem. Thermodyn., 1993, 25, 1461-94. [all data]
Schroeer, 1941
Schroeer, E.,
Critical State VI. Vapor-pressure Curve of Naphthalene Up To the Critical Point,
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Zhuravlev, 1937
Zhuravlev, D.I.,
Crit. Temp. and Orthobaric Density of Diphenyl Ether and Napphthalene naphthalene,
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Zhao, Unhannanant, et al., 2008
Zhao, Hui; Unhannanant, Patamaporn; Hanshaw, William; Chickos, James S.,
Enthalpies of Vaporization and Vapor Pressures of Some Deuterated Hydrocarbons. Liquid-Vapor Pressure Isotope Effects,
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Haftka, Parsons, et al., 2006
Haftka, Joris J.H.; Parsons, John R.; Govers, Harrie A.J.,
Supercooled liquid vapour pressures and related thermodynamic properties of polycyclic aromatic hydrocarbons determined by gas chromatography,
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Chickos, Hesse, et al., 1998
Chickos, James; Hesse, Donald; Hosseini, Sarah; Nichols, Gary; Webb, Paul,
Sublimation enthalpies at 298.15K using correlation gas chromatography and differential scanning calorimetry measurements,
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Chickos, Hosseini, et al., 1995
Chickos, James S.; Hosseini, Sarah; Hesse, Donald G.,
Determination of vaporization enthalpies of simple organic molecules by correlations of changes in gas chromatographic net retention times,
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Torres-Gomez, Barreiro-Rodriguez, et al., 1988
Torres-Gomez, L.A.; Barreiro-Rodriguez, G.; Galarza-Mondragon, A.,
A new method for the measurement of enthalpies of sublimation using differential scanning calorimetry,
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Lei, Chankalal, et al., 2002
Lei, Ying Duan; Chankalal, Raymond; Chan, Anita; Wania, Frank,
Supercooled Liquid Vapor Pressures of the Polycyclic Aromatic Hydrocarbons,
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Boller and Wiedemann, 1998
Boller, A.; Wiedemann, H.G.,
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Back, Grzyll, et al., 1996
Back, Dwight D.; Grzyll, Lawrence R.; Corrigan, Mary,
DSC enthalpy of vaporization measurements of high temperature two-phase working fluids,
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Lee and Holder, 1993
Lee, Chang Ha; Holder, Gerald D.,
Vapor-liquid equilibria in the systems toluene/naphthalene and cyclohexane/naphthalene,
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Ambrose, Ewing, et al., 1990
Ambrose, D.; Ewing, M.B.; Ghiassee, N.B.; Sanchez Ochoa, J.C.,
The ebulliometric method of vapour-pressure measurement: vapour pressures of benzene, hexafluorobenzene, and naphthalene,
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Stephenson and Malanowski, 1987
Stephenson, Richard M.; Malanowski, Stanislaw,
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de Kruif, Kuipers, et al., 1981
de Kruif, C.G.; Kuipers, T.; van Miltenburg, J.C.; Schaake, R.C.F.; Stevens, G.,
The vapour pressure of solid and liquid naphthalene,
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Wilson, Johnston, et al., 1981
Wilson, Grant M.; Johnston, Robert H.; Hwang, Shuen-Cheng.; Tsonopoulos, Constantine.,
Volatility of coal liquids at high temperatures and pressures,
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Fowler, Trump, et al., 1968
Fowler, Lewis.; Trump, Walter N.; Vogler, Carl E.,
Vapor pressure of naphthalene. Measurements between 40.deg. and 180.deg.,
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Notes
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- Symbols used in this document:
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) 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 ΔcH°solid Enthalpy of combustion of solid at standard conditions ΔfH°solid Enthalpy of formation of solid at standard conditions ΔfusH Enthalpy of fusion ΔfusS Entropy of fusion 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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