Naphthalene

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Gas phase thermochemistry data

Go To: Top, Phase change data, Henry's Law 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:
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
Δfgas150. ± 10.kJ/molAVGN/AAverage of 7 values; Individual data points

Constant pressure heat capacity of gas

Cp,gas (J/mol*K) Temperature (K) Reference Comment
36.1850.Thermodynamics Research Center, 1997p=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
47.50100.
63.89150.
84.99200.
120.52273.15
133.02298.15
133.94300.
181.16400.
220.70500.
252.37600.
277.77700.
298.43800.
315.50900.
329.771000.
341.81100.
352.01200.
360.81300.
368.21400.
374.71500.

Constant pressure heat capacity of gas

Cp,gas (J/mol*K) Temperature (K) Reference Comment
201.6 ± 2.0451.0Barrow G.M., 1951GT
226.7 ± 2.3522.7

Phase change data

Go To: Top, Gas phase thermochemistry data, Henry's Law 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:
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
Tboil490. ± 5.KAVGN/AAverage of 10 out of 11 values; Individual data points
Quantity Value Units Method Reference Comment
Tfus353.2 ± 0.7KAVGN/AAverage of 55 out of 57 values; Individual data points
Quantity Value Units Method Reference Comment
Ttriple353.39 ± 0.09KAVGN/AAverage of 6 values; Individual data points
Quantity Value Units Method Reference Comment
Tc748. ± 6.KAVGN/AAverage of 13 out of 14 values; Individual data points
Quantity Value Units Method Reference Comment
Pc41. ± 1.barAVGN/AAverage of 10 out of 11 values; Individual data points
Quantity Value Units Method Reference Comment
Vc0.407l/molN/ATsonopoulos and Ambrose, 1995 
Vc0.409l/molN/ACheng, 1963Uncertainty assigned by TRC = 0.06 l/mol; TRC
Quantity Value Units Method Reference Comment
ρc2.46 ± 0.05mol/lN/ATsonopoulos and Ambrose, 1995 
ρc2.497mol/lN/AChirico, Knipmeyer, et al., 1993Uncertainty assigned by TRC = 0.078 mol/l; TRC
ρc2.450mol/lN/ASchroeer, 1941Uncertainty assigned by TRC = 0.04 mol/l; TRC
ρc2.456mol/lN/AZhuravlev, 1937Uncertainty assigned by TRC = 0.04 mol/l; TRC
Quantity Value Units Method Reference Comment
Δvap54.6kJ/molCGCZhao, Unhannanant, et al., 2008AC
Δvap60.3 ± 1.1kJ/molGCHaftka, Parsons, et al., 2006Based on data from 333. to 403. K.; AC
Δvap53.4kJ/molCGCChickos, Hesse, et al., 1998AC
Δvap56.6kJ/molCGCChickos, Hosseini, et al., 1995Based on data from 403. to 453. K.; AC
Quantity Value Units Method Reference Comment
Δsub71. ± 5.kJ/molAVGN/AAverage of 17 values; Individual data points

Enthalpy of vaporization

ΔvapH (kJ/mol) Temperature (K) Method Reference Comment
70.850323.N/ATorres-Gomez, Barreiro-Rodriguez, et al., 1988DH
56.1398.GCLei, Chankalal, et al., 2002Based on data from 323. to 473. K.; AC
47.6 ± 1.8491. to 747.DSCBoller and Wiedemann, 1998AC
45.4475.DSCBack, Grzyll, et al., 1996Based on data from 460. to 647. K.; AC
48.7 ± 0.3400.EBChirico, Knipmeyer, et al., 1993, 2AC
46.4440.EBChirico, Knipmeyer, et al., 1993, 2AC
44.0480.EBChirico, Knipmeyer, et al., 1993, 2AC
41.5520.EBChirico, Knipmeyer, et al., 1993, 2AC
44.4528.N/ALee and Holder, 1993Based on data from 513. to 613. K.; AC
47.9423.EBAmbrose, Ewing, et al., 1990Based on data from 418. to 613. K.; AC
50.6367.AStephenson and Malanowski, 1987Based on data from 352. to 500. K.; AC
44.8506.AStephenson and Malanowski, 1987Based on data from 491. to 565. K.; AC
43.2578.AStephenson and Malanowski, 1987Based on data from 563. to 663. K.; AC
43.3676.AStephenson and Malanowski, 1987Based on data from 661. to 750. K.; AC
50.3 ± 0.2370.N/Ade Kruif, Kuipers, et al., 1981Based on data from 353. to 388. K.; AC
44.7466.N/AWilson, Johnston, et al., 1981Based on data from 441. to 727. K.; AC
50.7369.N/AFowler, Trump, et al., 1968Based on data from 354. to 453. K.; AC
49.0414.N/ACamin and Rossini, 1955Based on data from 399. to 491. K.; AC
46.4441.CBarrow and McClellan, 1951AC
48.3379.ICramer, 1943AC
47.2423.IMortimer and Murphy, 1923Based on data from 373. to 473. K.; AC
47.7427.INELSON and SENSEMAN, 1922Based on data from 360. to 494. K.; AC

Entropy of vaporization

ΔvapS (J/mol*K) Temperature (K) Reference Comment
219.3323.Torres-Gomez, Barreiro-Rodriguez, et al., 1988DH

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 452.304.271171831.571-61.329Fowler, Trump, et al., 1968Coefficents calculated by NIST from author's data.
399.47 to 491.793.970671606.529-85.923Camin and Rossini, 1955 

Enthalpy of sublimation

ΔsubH (kJ/mol) Temperature (K) Method Reference Comment
72.320298.15N/ATorres-Gomez, Barreiro-Rodriguez, et al., 1988DH
72.8327.GSGrayson and Fosbraey, 2006Based on data from 302. to 352. K.; AC
64. ± 0.5281. to 290.LEMcEachern and Sandoval, 2001AC
88.0 ± 2.5267. to 303.MEBoller and Wiedemann, 1998AC
71.7333.GSNass, Lenoir, et al., 1995Based on data from 313. to 353. K.; AC
73.7 ± 1.0258.GSWania, Shiu, et al., 1994Based on data from 243. to 273. K.; AC
78. ± 1.337. to 352.GCKhudyakov, 1988AC
71. ± 4.323.DSCTorres-Gomez, Barreiro-Rodriguez, et al., 1988AC
73.4315.GSSATO, INOMATA, et al., 1986Based on data from 299. to 331. K.; AC
72.3 ± 0.8293. to 331.QRGlukhova, Arkhangelova, et al., 1985AC
69.9333. to 393.GSMatsubara and Kuwamoto, 1985AC
75.8 ± 1.1303.GSSonnefeld, Zoller, et al., 1983Based on data from 283. to 323. K.; AC
72.8 ± 0.3271. to 285.MEColomina, Jimenez, et al., 1982AC
72.5 ± 0.1274. to 353.DMde Kruif, Kuipers, et al., 1981AC
72.6 ± 0.6253. to 273.TEKruif, 1980AC
76.0 ± 2.0328. to 398.DSCMurray, Cavell, et al., 1980AC
71.3293.GSMacknick and Prausnitz, 1979Based on data from 280. to 305. K.; AC
74.8 ± 0.4253. to 273.TEDe Kruif and Van Ginkel, 1977AC
73.9 ± 0.2253. to 273.MEDe Kruif and Van Ginkel, 1977AC
72.5 ± 0.3263. to 343.DMAmbrose, Lawrenson, et al., 1975AC
67.8 ± 3.5280.HSAChickos, 1975AC
74.4 ± 1.7303. to 329.TSGCMcEachern, Sandoval, et al., 1975AC
72.7 ± 1.7283.VRadchenko and Kitaigorodskii, 1974ALS
72.7283. to 323.MERadchenko, 1971AC
66.53 ± 0.84283.VKaryakin, Rabinovich, et al., 1968ALS
72.7 ± 0.3230. to 260.KGMiller, 1963See also Cox and Pilcher, 1970.; AC
66.3 ± 2.3354.7VAihara, 1959crystal phase; ALS
66.3276. to 283.VAihara, 1959, 2AC
69.2268.N/AHoyer and Peperle, 1958Based on data from 253. to 283. K.; AC
65.8293.EffusionSklyarenko, Markin, et al., 1958Based on data from 283. to 303. K.; AC
72.1292.N/ASherwood and Bryant, 1957Based on data from 273. to 311. K.; AC
72.4279. to 294.N/ABradley and Cleasby, 1953See also Jones, 1960 and Sears and Hopke, 1954.; AC
72.383279.7VBradley and Cleasby, 1953, 2ALS
65.7297.EffusionZibberman-Granovskaya, 1940Based on data from 288. to 306. K.; AC
76.6237. to 276.N/AAndrews, 1925AC
82.0293.MESwan and Mack, 1925Based on data from 283. to 303. K.; AC

Entropy of sublimation

ΔsubS (J/mol*K) Temperature (K) Reference Comment
242.6298.15Torres-Gomez, Barreiro-Rodriguez, et al., 1988DH

Enthalpy of fusion

ΔfusH (kJ/mol) Temperature (K) Method Reference Comment
18.811353.44N/AMastrangelo, 1957DH
18.226353.43N/AMcCullough, Finke, et al., 1957DH
19.200353.0N/ASpaght, Thomas, et al., 1932DH
19.1353.5DSCSharma, Gupta, et al., 2008AC
16.44353.8DSCHafsaoui and Mahmoud, 2007AC
19.55354.7DSCKhimeche and Dahmani, 2006AC
19.55354.7DSCKhimeche and Dahmani, 2006, 2AC
19.0353.4ACChirico, Knipmeyer, et al., 2002Based on data from 5. to 440. K.; AC
19.1353.4N/AAcree, 1991AC
19.020354.1N/ASyunyaev, Tumanyan, et al., 1984Relative error in determination ± 5%.; DH
19.100353.5N/ARastogi and Bassi, 1964DH
18.785353.N/AUeberreiter and Orthmann, 1950DH
18.790353.4N/AEibert, 1944DH
19.040353.4N/ASchmidt, 1941DH
19.000353.1N/AAndrews, Lynn, et al., 1926DH
19.250353.N/ADavid, 1964Temperature not measured.; DH

Entropy of fusion

ΔfusS (J/mol*K) Temperature (K) Reference Comment
51.57353.43McCullough, Finke, et al., 1957DH
54.4353.0Spaght, Thomas, et al., 1932DH
53.7354.1Syunyaev, Tumanyan, et al., 1984Relative; DH
54.0353.5Rastogi and Bassi, 1964DH
53.2353.Ueberreiter and Orthmann, 1950DH
53.2353.4Eibert, 1944DH
53.9353.4Schmidt, 1941DH
53.8353.1Andrews, Lynn, et al., 1926DH
55.353.David, 1964Temperature; DH

Enthalpy of phase transition

ΔHtrs (kJ/mol) Temperature (K) Initial Phase Final Phase Reference Comment
19.046353.376crystaline, IliquidAndon and Connett, 1980DH
19.000353.8crystaline, IliquidRadomska and Radomski, 1980DH

Entropy of phase transition

ΔStrs (J/mol*K) Temperature (K) Initial Phase Final Phase Reference Comment
53.90353.376crystaline, IliquidAndon and Connett, 1980DH
53.70353.8crystaline, IliquidRadomska and Radomski, 1980DH

In addition to the Thermodynamics Research Center (TRC) data available from this site, much more physical and chemical property data is available from the following TRC products:


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) = H exp(d(ln(kH))/d(1/T) ((1/T) - 1/(298.15 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)

H (mol/(kg*bar)) d(ln(kH))/d(1/T) (K) Method Reference Comment
0.80 QN/A missing citation give several references for the Henry's law constants but don't assign them to specific species.
2.0 XN/A 
2.13600.XN/A 
2.4 LN/A 
2.1 MMackay, Shiu, et al., 1979 
2.1 TMackay, Shiu, et al., 1979 
2.4 VN/A 
1.9 VBohon and Claussen, 1951 

Gas phase ion energetics data

Go To: Top, Gas phase thermochemistry data, Phase change data, Henry's Law data, References, Notes

Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.

Data 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
MM - Michael M. Meot-Ner (Mautner)
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 C10H8+ (ion structure unspecified)

Quantity Value Units Method Reference Comment
IE (evaluated)8.144 ± 0.001eVN/AN/AL
Quantity Value Units Method Reference Comment
Proton affinity (review)802.9kJ/molN/AHunter and Lias, 1998HL
Quantity Value Units Method Reference Comment
Gas basicity779.4kJ/molN/AHunter and Lias, 1998HL

Electron affinity determinations

EA (eV) Method Reference Comment
-0.2LPESLyapustina, Xu, et al., 2000Extrapolated from EAs of solvation series naphthalene-...(H2O)n; B
-0.18N/ASong, Han, et al., 2002Extrapolated from LPES EAs of (naphthalene)n; B
-0.200 ± 0.050LPESSchiedt, Knott, et al., 2000Extrapolated from EAs of (H2O)n..naphthalene-. series; B
-0.1908ETSBurrow, Michejda, et al., 1987The question of whether the naphthalene radical anion is bound or not has not been settled; B
0.140 ± 0.050ECDZlatkis, Lee, et al., 1983However, see Heinis, Chowdhury, et al., 1993 for a discussion; it may not be bound.; B
<0.134 ± 0.043ECDWojnarovits and Foldiak, 1981EA is an upper limit: Chen and Wentworth, 1989. G3MP2B3 calculations indicate an EA of ca. -0.3 eV, anion unbound.; B
0.1480 ± 0.0060ECDBecker and Chen, 1966B

Proton affinity at 298K

Proton affinity (kJ/mol) Reference Comment
800.0Aue, Guidoni, et al., 2000Experimental literature data re-evaluated by the authors using ab initio protonation entropies; MM

Gas basicity at 298K

Gas basicity (review) (kJ/mol) Reference Comment
774.5Aue, Guidoni, et al., 2000Experimental literature data re-evaluated by the authors using ab initio protonation entropies; MM

Ionization energy determinations

IE (eV) Method Reference Comment
8.12 ± 0.02TRPIGotkis, Oleinikova, et al., 1993LL
8.1442 ± 0.0009TECockett, Ozeki, et al., 1993LL
8.12 ± 0.01PIJochims, Rasekh, et al., 1992LL
8.14EIStahl and Maquin, 1984LBLHLM
8.141 ± 0.001LSDuncan, Dietz, et al., 1981LLK
8.08 ± 0.05EQMautner(Meot-Ner), 1980LLK
8.15PESchafer, Schweig, et al., 1975LLK
8.15PESchafer, Schweig, et al., 1973LLK
8.12CTSPitt, 1973LLK
8.15PEClark, Brogli, et al., 1972LLK
8.13PEBrundle, Robin, et al., 1972LLK
8.15PEBrogli, Heilbronner, et al., 1972LLK
8.16 ± 0.03EIJohnstone, Mellon, et al., 1970RDSH
8.11 ± 0.01PEDewar and Worley, 1969RDSH
8.15 ± 0.01PIYencha and El-Sayed, 1968RDSH
8.133SKitagawa, 1968RDSH
8.14PIKitagawa, 1968RDSH
8.12 ± 0.05PEEland and Danby, 1968RDSH
8.136 ± 0.005SAngus, Christ, et al., 1968RDSH
8.25 ± 0.01EIBonnier, Gelus, et al., 1965RDSH
8.15CTSKuroda, 1964RDSH
8.16CTSBriegleb, 1964RDSH
8.08CTSKinoshita, 1962RDSH
8.1PITerenin, 1961RDSH
8.10CTSBirks and Stifkin, 1961RDSH
8.12 ± 0.01PIWatanabe, 1957RDSH
8.14 ± 0.02PIVilesov and Terenin, 1957RDSH
8.09PEKlasinc, Kovac, et al., 1983Vertical value; LBLHLM
8.15PEKaim, Tesmann, et al., 1980Vertical value; LLK
8.15 ± 0.02PESchmidt, 1977Vertical value; LLK
8.18 ± 0.03PEHeilbronner, Hoshi, et al., 1976Vertical value; LLK
8.15PEClar and Schmidt, 1976Vertical value; LLK
8.31 ± 0.03PEMarschner and Goetz, 1974Vertical value; LLK
8.15PEBock, Wagner, et al., 1972Vertical value; LLK
8.15PEBock and Wagner, 1972Vertical value; LLK

Appearance energy determinations

Ion AE (eV) Other Products MethodReferenceComment
C3H3+19.35?PIJochims, Rasekh, et al., 1993LL
C3H3+19.2 ± 0.1C3H3+C4H2PIJochims, Rasekh, et al., 1992LL
C4H2+20.7 ± 0.13C2H2PIJochims, Rasekh, et al., 1992LL
C4H3+22.3 ± 0.12C2H2+C2HPIJochims, Rasekh, et al., 1992LL
C4H4+19.4 ± 0.1C4H2+C2H2PIJochims, Rasekh, et al., 1992LL
C4H4+19.6 ± 0.20?EIVanBrunt and Wacks, 1964RDSH
C5H3+19.74?PIJochims, Rasekh, et al., 1993LL
C5H3+19.7 ± 0.1C2H2+C3H3PIJochims, Rasekh, et al., 1992LL
C6H3+20.77 ± 0.01?EIVanBrunt and Wacks, 1964RDSH
C6H4+18.7 ± 0.12C2H2PIJochims, Rasekh, et al., 1992LL
C6H4+18.2 ± 0.15?EIVanBrunt and Wacks, 1964RDSH
C6H5+18.72?PIJochims, Rasekh, et al., 1993LL
C6H5+18.6 ± 0.1C2H2+C2HPIJochims, Rasekh, et al., 1992LL
C6H5+18.45 ± 0.05?EIVanBrunt and Wacks, 1964RDSH
C6H6+15.64C4H2PIJochims, Rasekh, et al., 1993LL
C6H6+15.7 ± 0.1C4H2PIJochims, Rasekh, et al., 1992LL
C6H6+15.20 ± 0.05?EIVanBrunt and Wacks, 1964RDSH
C7H3+20.66 ± 0.15C3H3+H2PIJochims, Rasekh, et al., 1992LL
C7H5+15.90C3H3PIJochims, Rasekh, et al., 1993LL
C7H5+16.1 ± 0.1C3H3PIJochims, Rasekh, et al., 1992LL
C8H5+19.00 ± 0.05C2H2+HPIJochims, Rasekh, et al., 1992LL
C8H5+18.07 ± 0.05?EIVanBrunt and Wacks, 1964RDSH
C8H6+15.50C2H2PIJochims, Rasekh, et al., 1993LL
C8H6+12.74C2H2EVALGotkis, Oleinikova, et al., 1993T = 0K; LL
C8H6+14.43C2H2TRPIGotkis, Oleinikova, et al., 1993LL
C8H6+15.4 ± 0.1C2H2PIJochims, Rasekh, et al., 1992LL
C8H6+15.4 ± 0.10C2H2EIVanBrunt and Wacks, 1964RDSH
C10H6+15.60 ± 0.05H2PIJochims, Rasekh, et al., 1992LL
C10H6+16.2 ± 0.15H2EIVanBrunt and Wacks, 1964RDSH
C10H7+15.41HPIJochims, Rasekh, et al., 1993LL
C10H7+12.37HEVALGotkis, Oleinikova, et al., 1993T = 0K; LL
C10H7+14.24HTRPIGotkis, Oleinikova, et al., 1993LL
C10H7+15.4 ± 0.1HPIJochims, Rasekh, et al., 1992LL
C10H7+15.4 ± 0.10HEIVanBrunt and Wacks, 1964RDSH

De-protonation reactions

C10H7- + Hydrogen cation = Naphthalene

By formula: C10H7- + H+ = C10H8

Quantity Value Units Method Reference Comment
Δr1649. ± 5.0kJ/molBranReed and Kass, 2000gas phase; B
Δr1649. ± 5.0kJ/molTDEqMeot-ner, Liebman, et al., 1988gas phase; anchored to 88MEO scale, not the "87 acidity scale". The Kiefer, Zhang, et al., 1997 BDE is for ortho.; B
Δr1648. ± 21.kJ/molCIDCLardin, Squires, et al., 2001gas phase; B
Quantity Value Units Method Reference Comment
Δr1613. ± 5.4kJ/molH-TSReed and Kass, 2000gas phase; B
Δr1606. ± 5.0kJ/molTDEqMeot-ner, Liebman, et al., 1988gas phase; anchored to 88MEO scale, not the "87 acidity scale". The Kiefer, Zhang, et al., 1997 BDE is for ortho.; B
Δr1613. ± 21.kJ/molH-TSLardin, Squires, et al., 2001gas phase; B

C10H7- + Hydrogen cation = Naphthalene

By formula: C10H7- + H+ = C10H8

Quantity Value Units Method Reference Comment
Δr1655. ± 5.4kJ/molBranReed and Kass, 2000gas phase; B
Quantity Value Units Method Reference Comment
Δr1619. ± 5.9kJ/molH-TSReed and Kass, 2000gas phase; B

References

Go To: Top, Gas phase thermochemistry data, Phase change data, Henry's Law 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.

Thermodynamics Research Center, 1997
Thermodynamics Research Center, Selected Values of Properties of Chemical Compounds., Thermodynamics Research Center, Texas A&M University, College Station, Texas, 1997. [all data]

Dorofeeva O.V., 1986
Dorofeeva O.V., On calculation of thermodynamic properties of polycyclic aromatic hydrocarbons, Thermochim. Acta, 1986, 102, 59-66. [all data]

Dorofeeva O.V., 1988
Dorofeeva O.V., Thermodynamic Properties of Polycyclic Aromatic Hydrocarbons in the Gaseous Phase. Institute for High Temperatures, USSR Academy of Sciences, Preprint No.1-238 (in Russian), Moscow, 1988. [all data]

Barrow G.M., 1951
Barrow G.M., The thermodynamic properties of naphthalene, J. Am. Chem. Soc., 1951, 73, 573-575. [all data]

McClellan A.L., 1955
McClellan A.L., Vibrational assignment and thermodynamic properties of naphthalene, J. Chem. Phys., 1955, 23, 245-248. [all data]

Lielmezs J., 1981
Lielmezs J., Jr., Thermodynamic functions for naphthalene, Thermochim. Acta, 1981, 47, 287-308. [all data]

Tsonopoulos and Ambrose, 1995
Tsonopoulos, C.; Ambrose, D., Vapor-Liquid Critical Properties of Elements and Compounds. 3. Aromatic Hydrocarbons, J. Chem. Eng. Data, 1995, 40, 547-558. [all data]

Cheng, 1963
Cheng, D.C.H., Critical temperatures and volumes of some binary systems, Chem. Eng. Sci., 1963, 18, 715. [all data]

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, 1461-94. [all data]

Schroeer, 1941
Schroeer, E., Critical State VI. Vapor-pressure Curve of Naphthalene Up To the Critical Point, Z. Phys. Chem., Abt. B, 1941, 49, 271-8. [all data]

Zhuravlev, 1937
Zhuravlev, D.I., Crit. Temp. and Orthobaric Density of Diphenyl Ether and Napphthalene naphthalene, Zh. Fiz. Khim., 1937, 9, 875. [all data]

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, J. Chem. Eng. Data, 2008, 53, 7, 1545-1556, https://doi.org/10.1021/je800091s . [all data]

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, Journal of Chromatography A, 2006, 1135, 1, 91-100, https://doi.org/10.1016/j.chroma.2006.09.050 . [all data]

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Notes

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