Benzoic acid

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Gas phase thermochemistry 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: Glushko Thermocenter, Russian Academy of Sciences, Moscow

Constant pressure heat capacity of gas

Cp,gas (J/mol*K) Temperature (K) Reference Comment
103.47298.15Stull D.R., 1969These values were calculated from preliminary assignment of vibrational frequencies. Statistical calculation [ Ali N., 1983] seems to be erroneous.
104.01300.
138.36400.
170.54500.
196.73600.
217.82700.
234.89800.
248.95900.
260.661000.

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, 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
Δcliquid-3227.00 ± 0.20kJ/molCcbGundry, Harrop, et al., 1969Reanalyzed by Pedley, Naylor, et al., 1986, Original value = -3225.73 kJ/mol; Corresponding Δfliquid = -385.06 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS
Quantity Value Units Method Reference Comment
Δfsolid-384.8 ± 0.50kJ/molCcbCorral, 1960ALS
Δfsolid-386.kJ/molCcbLandrieu, Baylocq, et al., 1929ALS
Quantity Value Units Method Reference Comment
Δcsolid-3228. ± 4.kJ/molAVGN/AAverage of 17 out of 18 values; Individual data points
Quantity Value Units Method Reference Comment
solid,1 bar165.71J/mol*KN/AKaji, Tochigi, et al., 1993DH
solid,1 bar167.73J/mol*KN/AArvidsson, Falk, et al., 1976DH
solid,1 bar167.59J/mol*KN/AFurukawa, McCoskey, et al., 1951DH
solid,1 bar167.82J/mol*KN/ADavies and Staveley, 1957DH
solid,1 bar170.7J/mol*KN/AParks, Huffman, et al., 1933Extrapolation below 90 K, 59.25 J/mol*K.; DH

Constant pressure heat capacity of liquid

Cp,liquid (J/mol*K) Temperature (K) Reference Comment
259.413.Pacor, 1967DH

Constant pressure heat capacity of solid

Cp,solid (J/mol*K) Temperature (K) Reference Comment
147.78300.Kaji, Tochigi, et al., 1993T = 19 to 312 K. Unsmoothed experimental datum.; DH
147.03298.902Sorai, Kaji, et al., 1992T = 15 to 305 K. Unsmoothed experimental datum.; DH
146.23296.29Moriya, Matsuo, et al., 1982T = 13 to 355 K. NBS SRM 29.; DH
146.65298.15Shakirov and Lyubarskii, 1980T = 20 to 300 K.; DH
146.79298.15Arvidsson, Falk, et al., 1976T = 6 to 341 K.; DH
147.07299.62Tatsumi, Matsuo, et al., 1975T = 12 to 304 K.; DH
149.301.Mosselman, Mourik, et al., 1974One temperature, T = 5 K. Value 5 J/mol*K.; DH
146.80298.15Konicek, Suurkuusk, et al., 1971DH
167.40298.15Justice, 1969As check on system. Only value at 298 K given.; DH
147.14299.99Suga and Seki, 1965T = 13 to 300 K. Value is unsmoothed experimental datum.; DH
130.340.David, 1964T = 298 to 373 K. Mean value. T = uncertain.; DH
146.31298.15Kolesov, Seregin, et al., 1962T = 22 to 310 K.; DH
147.02298.15Davies and Staveley, 1957T = 20 to 298 K.; DH
149.79298.15Popov and Kolesov, 1956T = 80 to 300 K.; DH
146.81298.15Ginnings and Furukawa, 1953T = 14 to 410 K.; DH
146.81298.15Furukawa, McCoskey, et al., 1951T = 13 to 410 K.; DH
160.2323.Satoh and Sogabe, 1939T = 0 to 100 C. Mean value.; DH
145.10295.1Parks, Huffman, et al., 1933T = 93 to 295 K. Value is unsmoothed experimental datum.; DH
155.2298.Andrews, Lynn, et al., 1926T = 22 to 200 C.; DH

Phase change 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 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
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein

Quantity Value Units Method Reference Comment
Tboil522.2KN/AWeast and Grasselli, 1989BS
Tboil522.KN/ABuckingham and Donaghy, 1982BS
Tboil523.18KN/ABurriel, 1931Uncertainty assigned by TRC = 0.2 K; TRC
Tboil523.59KN/ABurriel, 1931Uncertainty assigned by TRC = 0.2 K; TRC
Quantity Value Units Method Reference Comment
Tfus395.2 ± 0.7KAVGN/AAverage of 18 out of 20 values; Individual data points
Quantity Value Units Method Reference Comment
Ttriple395.52KN/AMarsh, 1987Uncertainty assigned by TRC = 0.005 K; recommended as calibration standard; TRC
Ttriple395.520KN/AAndon and Connett, 1980Uncertainty assigned by TRC = 0.01 K; TRC
Ttriple395.52KN/AGinnings and Furukawa, 1953, 2Uncertainty assigned by TRC = 0.01 K; TRC
Ttriple395.52KN/AFurukawa, McCoskey, et al., 1951, 2Uncertainty assigned by TRC = 0.01 K; TRC
Quantity Value Units Method Reference Comment
Δvap78.9kJ/molCGCChickos, Hosseini, et al., 1995Based on data from 353. to 393. K.; AC
Quantity Value Units Method Reference Comment
Δsub90. ± 4.kJ/molAVGN/AAverage of 13 values; Individual data points

Reduced pressure boiling point

Tboil (K) Pressure (bar) Reference Comment
406.20.013Weast and Grasselli, 1989BS
406.0.013Buckingham and Donaghy, 1982BS

Enthalpy of vaporization

ΔvapH (kJ/mol) Temperature (K) Method Reference Comment
87.450335.N/ATorres-Gomez, Barreiro-Rodriguez, et al., 1988DH
63.3 ± 0.6401. to 416.N/APena, Ribet, et al., 2003AC
66.3420.AStephenson and Malanowski, 1987Based on data from 405. to 523. K.; AC
67.8368. to 428.GSMatsubara and Kuwamoto, 1985AC
65.4428.ICramer, 1943AC
67.7416.MM,AKlosky, Woo, et al., 1927Based on data from 401. to 520. K.; AC

Entropy of vaporization

ΔvapS (J/mol*K) Temperature (K) Reference Comment
261.0335.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
369. to 522.44.478341771.357-127.484Stull, 1947Coefficents calculated by NIST from author's data.

Enthalpy of sublimation

ΔsubH (kJ/mol) Temperature (K) Method Reference Comment
89.230298.15N/ATorres-Gomez, Barreiro-Rodriguez, et al., 1988DH
90.9 ± 2.0340. to 410.TG-TSSelvakumar, Raghunathan, et al., 2009AC
90.0 ± 0.5307.MERibeiro da Silva, Monte, et al., 2006Based on data from 299. to 317. K.; AC
93. ± 4.294. to 331.MEGinkel, Kruif, et al., 2001AC
90.5 ± 0.3323. to 394.GSZielenkiewicz, Perlovich, et al., 1999AC
86.7313. to 343.TGAElder, 1997AC
88.7 ± 0.9311.MEDa Silva and Monte, 1990Based on data from 307. to 314. K.; AC
87.5 ± 0.3335.CTorres-Gomez, Barreiro-Rodriguez, et al., 1988AC
90.8 ± 0.6306.QRGlukhova, Arkhangelova, et al., 1985Based on data from 293. to 319. K.; AC
95.1 ± 1.8294.N/AKaisersberger, Hädrich, et al., 1985AC
87.8368. to 428.GSMatsubara and Kuwamoto, 1985AC
91. ± 2.293. to 313.MEColomina, Jimenez, et al., 1982AC
89.5 ± 0.05353.DMde Kruif and Blok, 1982Based on data from 316. to 391. K.; AC
89.1 ± 0.2320. to 370.CMurata, Sakiyama, et al., 1982AC
85. ± 2.369.SGSachinidis and Hill, 1980Based on data from 344. to 395. K.; AC
88.3 ± 2.9281. to 323.LENowak, Szczepaniak, et al., 1978AC
88.5 ± 1.6293. to 318.TEDeKruif, van Ginkel, et al., 1975AC
92.9 ± 0.2296.MEArshadi, 1974Based on data from 273. to 318. K.; AC
88.1 ± 0.2293. to 311.TCMde Kruif and Oonk, 1973AC
89.0 ± 0.4338. to 383.MEMalaspina, 1973AC
89.3 ± 0.4338. to 383.CMalaspina, 1973AC
90. ± 0.3293. to 308.MEColomina, Monzon, et al., 1972AC
86.6 ± 1.3290. to 315.ME,CWiedemann, 1972AC
89.1314.N/AAshcroft, 1971Based on data from 299. to 329. K.; AC
90.4 ± 0.8367.HSAMelia and Merrifield, 1970Based on data from 324. to 392. K.; AC
86.6 ± 1.7303.MEWiedemann and Waughna, 1970Based on data from 290. to 315. K. See also Zielenkiewicz, Perlovich, et al., 1999.; AC
88.9 ± 0.5363.GSMertl, 1968Based on data from 348. to 378. K.; AC
90.9299.MEDavies and Kybett, 1965Based on data from 291. to 307. K.; AC
84.2 ± 0.8318.TEWolf and Weghofer, 1938AC
84.1 ± 0.8318.VWolf and Weghofer, 1938, 2ALS
85.8383.THirsbrunner, 1934Based on data from 333. to 389. K.; AC
84.5 ± 0.5364.IKlosky, Woo, et al., 1927Based on data from 377. to 394. K.; AC

Entropy of sublimation

ΔsubS (J/mol*K) Temperature (K) Reference Comment
299.3298.15Torres-Gomez, Barreiro-Rodriguez, et al., 1988DH

Enthalpy of fusion

ΔfusH (kJ/mol) Temperature (K) Method Reference Comment
18.006395.52N/AGinnings and Furukawa, 1953DH
18.000395.52N/AFurukawa, McCoskey, et al., 1951DH
16.99396.9DSCBrittain, 2009AC
17.3394.4DSCSharma, Kant, et al., 2003See also Sharma, Jamwal, et al., 2004.; AC
17.1395.4DSCRoy, Riga, et al., 2002AC
17.99395.5N/APitzer, Peiper, et al., 1984AC
16.230395.N/APacor, 1967DH
17.320395.0N/AAndrews, Lynn, et al., 1926DH
17.400395.N/ADavid, 1964Temperature not measured.; DH

Entropy of fusion

ΔfusS (J/mol*K) Temperature (K) Reference Comment
45.52395.52Ginnings and Furukawa, 1953DH
45.51395.52Furukawa, McCoskey, et al., 1951DH
41.1395.Pacor, 1967DH
43.8395.0Andrews, Lynn, et al., 1926DH
44.395.David, 1964Temperature; DH

Enthalpy of phase transition

ΔHtrs (kJ/mol) Temperature (K) Initial Phase Final Phase Reference Comment
18.062395.527crystaline, IliquidAndon and Connett, 1980, 2DH

Entropy of phase transition

ΔStrs (J/mol*K) Temperature (K) Initial Phase Final Phase Reference Comment
45.67395.527crystaline, IliquidAndon and Connett, 1980, 2DH

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:


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, 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

benzoate anion + Hydrogen cation = Benzoic acid

By formula: C7H5O2- + H+ = C7H6O2

Quantity Value Units Method Reference Comment
Δr1423. ± 9.2kJ/molG+TSFujio, McIver, et al., 1981gas phase; value altered from reference due to change in acidity scale; B
Δr1423. ± 12.kJ/molG+TSCumming and Kebarle, 1978gas phase; Recalculated from data in paper; error in Table vs. ladder; B
Δr1423. ± 9.2kJ/molG+TSCaldwell, Renneboog, et al., 1989gas phase; B
Quantity Value Units Method Reference Comment
Δr1393. ± 8.4kJ/molIMREFujio, McIver, et al., 1981gas phase; value altered from reference due to change in acidity scale; B
Δr1393. ± 8.4kJ/molIMRECumming and Kebarle, 1978gas phase; Recalculated from data in paper; error in Table vs. ladder; B
Δr1394. ± 8.4kJ/molIMRECaldwell, Renneboog, et al., 1989gas phase; B

Bromine anion + Benzoic acid = (Bromine anion • Benzoic acid)

By formula: Br- + C7H6O2 = (Br- • C7H6O2)

Quantity Value Units Method Reference Comment
Δr76.6 ± 7.5kJ/molIMREPaul and Kebarle, 1991gas phase; ΔGaff measured at 423 K, ΔSaff taken as that of PhNO2..Br-; B,M
Quantity Value Units Method Reference Comment
Δr84.J/mol*KN/APaul and Kebarle, 1991gas phase; Entropy change calculated or estimated; M
Quantity Value Units Method Reference Comment
Δr41. ± 4.2kJ/molIMREPaul and Kebarle, 1991gas phase; ΔGaff measured at 423 K, ΔSaff taken as that of PhNO2..Br-; B

Free energy of reaction

ΔrG° (kJ/mol) T (K) Method Reference Comment
41.423.PHPMSPaul and Kebarle, 1991gas phase; Entropy change calculated or estimated; M

Water + Benzoyl chloride = Benzoic acid + Hydrogen chloride

By formula: H2O + C7H5ClO = C7H6O2 + HCl

Quantity Value Units Method Reference Comment
Δr-34.04 ± 0.21kJ/molCmMoselhy and Pritchard, 1975liquid phase; solvent: Diphenyl-ether; see Carson, Pritchard, et al., 1950 and Davies, Dunning, et al., 1972; ALS
Δr-101.9kJ/molCmCarson, Pritchard, et al., 1950liquid phase; Heat of hydrolysis; ALS

Benzaldehyde + perbenzoic acid = 2Benzoic acid

By formula: C7H6O + C7H6O3 = 2C7H6O2

Quantity Value Units Method Reference Comment
Δr-316. ± 13.kJ/molCmBriner and Chastonay, 1954liquid phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -317. ± 13. kJ/mol; ALS

Benzoyl bromide + Water = Hydrogen bromide + Benzoic acid

By formula: C7H5BrO + H2O = HBr + C7H6O2

Quantity Value Units Method Reference Comment
Δr-113.1kJ/molCmCarson, Pritchard, et al., 1950liquid phase; Heat of hydrolysis; ALS

Benzoyl iodide + Water = Hydrogen iodide + Benzoic acid

By formula: C7H5IO + H2O = HI + C7H6O2

Quantity Value Units Method Reference Comment
Δr-102.4kJ/molCmCarson, Pritchard, et al., 1950liquid phase; Heat of hydrolysis; ALS

Water + Benzoic acid, methyl ester = Benzoic acid + Methyl Alcohol

By formula: H2O + C8H8O2 = C7H6O2 + CH4O

Quantity Value Units Method Reference Comment
Δr-73.0 ± 1.9kJ/molEqkGuthrie and Cullimore, 1980liquid phase; ALS

Henry's Law data

Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Gas phase ion energetics data, Ion clustering 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 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
24000. QN/A missing citation give several references for the Henry's law constants but don't assign them to specific species.
14000.6500.XN/A 

Gas phase ion energetics data

Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Henry's Law data, Ion clustering 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

Data compiled as indicated in comments:
B - John E. Bartmess
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

Quantity Value Units Method Reference Comment
Proton affinity (review)821.1kJ/molN/AHunter and Lias, 1998HL
Quantity Value Units Method Reference Comment
Gas basicity790.1kJ/molN/AHunter and Lias, 1998HL

Ionization energy determinations

IE (eV) Method Reference Comment
9.3PEKlasinc, Kovac, et al., 1983LBLHLM
9.6PEMeeks, Wahlborg, et al., 1981LLK
9.8 ± 0.2EIBenoit, 1973LLK
9.75EIBenoit, 1973, 2LLK
9.73 ± 0.09EIFoffani, Pignataro, et al., 1964RDSH
9.47PEKlasinc, Kovac, et al., 1983Vertical value; LBLHLM

Appearance energy determinations

Ion AE (eV) Other Products MethodReferenceComment
C6H5+14.3 ± 0.07?EITajima, Azami, et al., 1977LLK
C6H5+15.1 ± 0.2CO+OHEIBenoit, 1973LLK
C6H5+15.08CO+OHEIBenoit, 1973, 2LLK
C7H5O+11.5 ± 0.07OHEITajima, Azami, et al., 1977LLK
C7H5O+12.1 ± 0.2OHEIBenoit, 1973LLK
C7H5O+12.11OHEIBenoit, 1973, 2LLK

De-protonation reactions

benzoate anion + Hydrogen cation = Benzoic acid

By formula: C7H5O2- + H+ = C7H6O2

Quantity Value Units Method Reference Comment
Δr1423. ± 9.2kJ/molG+TSFujio, McIver, et al., 1981gas phase; value altered from reference due to change in acidity scale; B
Δr1423. ± 12.kJ/molG+TSCumming and Kebarle, 1978gas phase; Recalculated from data in paper; error in Table vs. ladder; B
Δr1423. ± 9.2kJ/molG+TSCaldwell, Renneboog, et al., 1989gas phase; B
Quantity Value Units Method Reference Comment
Δr1393. ± 8.4kJ/molIMREFujio, McIver, et al., 1981gas phase; value altered from reference due to change in acidity scale; B
Δr1393. ± 8.4kJ/molIMRECumming and Kebarle, 1978gas phase; Recalculated from data in paper; error in Table vs. ladder; B
Δr1394. ± 8.4kJ/molIMRECaldwell, Renneboog, et al., 1989gas phase; B

Ion clustering data

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, 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

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

Bromine anion + Benzoic acid = (Bromine anion • Benzoic acid)

By formula: Br- + C7H6O2 = (Br- • C7H6O2)

Quantity Value Units Method Reference Comment
Δr76.6 ± 7.5kJ/molIMREPaul and Kebarle, 1991gas phase; ΔGaff measured at 423 K, ΔSaff taken as that of PhNO2..Br-; B,M
Quantity Value Units Method Reference Comment
Δr84.J/mol*KN/APaul and Kebarle, 1991gas phase; Entropy change calculated or estimated; M
Quantity Value Units Method Reference Comment
Δr41. ± 4.2kJ/molIMREPaul and Kebarle, 1991gas phase; ΔGaff measured at 423 K, ΔSaff taken as that of PhNO2..Br-; B

Free energy of reaction

ΔrG° (kJ/mol) T (K) Method Reference Comment
41.423.PHPMSPaul and Kebarle, 1991gas phase; Entropy change calculated or estimated; M

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, Notes

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

Stull D.R., 1969
Stull D.R., Jr., The Chemical Thermodynamics of Organic Compounds. Wiley, New York, 1969. [all data]

Ali N., 1983
Ali N., Thermodynamic functions of the benzoic acid, phthalic acid and salicylic acid, Indian J. Phys., 1983, B57, 413-419. [all data]

Gundry, Harrop, et al., 1969
Gundry, H.A.; Harrop, D.; Head, A.J.; Lewis, G.B., Thermodynamic properties of organic oxygen compounds. 21. Enthalpies of combustion of benzoic acid, pentan-1-ol, octan-1-ol, and hexadecan-1-ol, J. Chem. Thermodyn., 1969, 1, 321-332. [all data]

Pedley, Naylor, et al., 1986
Pedley, J.B.; Naylor, R.D.; Kirby, S.P., Thermochemical Data of Organic Compounds, Chapman and Hall, New York, 1986, 1-792. [all data]

Corral, 1960
Corral, L.B., Investigaciones termoquimicas sobre los acidos toluicos y dimetilbenzoicos, Rev. R. Acad. Cienc., 1960, 54, 365-403. [all data]

Landrieu, Baylocq, et al., 1929
Landrieu, P.; Baylocq, F.; Johnson, J.R., Etude thermochimique dans la serie furanique, Bull. Soc. Chim. France, 1929, 45, 36-49. [all data]

Kaji, Tochigi, et al., 1993
Kaji, K.; Tochigi, K.; Misawa, Y.; Suzuki, T., An adiabatic calorimeter for samples of mass less than 0.1 g and heat capacity measurements on benzoic acid at temperatures from 19 K to 312 K, J. Chem. Thermodynam., 1993, 25(6), 699-709. [all data]

Arvidsson, Falk, et al., 1976
Arvidsson, K.; Falk, B.; Sunner, S., A small sample low temperature adiabatic heat capacity calorimeter with an automatic data acquisition system, Chem. Scr., 1976, 10, 193-200. [all data]

Furukawa, McCoskey, et al., 1951
Furukawa, G.T.; McCoskey, R.E.; King, G.J., Calorimetric properties of benzoic acid from 0 to 410K, J. Res., 1951, NBS 47, 256-261. [all data]

Davies and Staveley, 1957
Davies, T.; Staveley, L.A.K., The behaviour of the ammonium ion in the ammonium salt of tetraphenylboron by comparison of the heat capacities of the ammonium, rubidium, and potassium salts, Trans. Faraday Soc., 1957, 53, 19-30. [all data]

Parks, Huffman, et al., 1933
Parks, G.S.; Huffman, H.M.; Barmore, M., Thermal data on organic compounds. XI. The heat capacities, entropies and free energies of ten compounds containing oxygen or nitrogen. J. Am. Chem. Soc., 1933, 55, 2733-2740. [all data]

Pacor, 1967
Pacor, P., Applicability of the DuPont 900 DTA apparatus in quantitative differential thermal analysis, Anal. Chim. Acta, 1967, 37, 200-208. [all data]

Sorai, Kaji, et al., 1992
Sorai, M.; Kaji, K.; Kaneko, Y., An automated adiabatic calorimeter for the temperature range 13 K to 530 K The heat capacities for benzoic acid from 15 K to 305 K and of synthetic sapphire from 60 K to 505 K, J. Chem. Thermodynam., 1992, 24(2), 167-180. [all data]

Moriya, Matsuo, et al., 1982
Moriya, K.; Matsuo, T.; Suga, H., Low temperature adiabatic calorimeter with a built-in cryo-refrigerator, J. Chem. Thermodynam., 1982, 14, 1143-1148. [all data]

Shakirov and Lyubarskii, 1980
Shakirov, R.F.; Lyubarskii, M.V., Low-temperature heat capacity and thermodynamic functions of methyl trichlorothioacrylate, SPSTL Deposited Publication 3 KhP-D80, 1980, 19p. [all data]

Tatsumi, Matsuo, et al., 1975
Tatsumi, M.; Matsuo, T.; Suga, H.; Seki, S., An adiabatic calorimeter for high-resolution heat capacity measurements in the temperature range from 12 to 300 K, Bull. Chem. Soc. Japan, 1975, 48, 3060-3066. [all data]

Mosselman, Mourik, et al., 1974
Mosselman, C.; Mourik, J.; Dekker, H., Enthalpies of phase change and heat capacities of some long-chain alcohols. Adiabatic semi-microcalorimeter for studies of polymorphism, J. Chem. Thermodynam., 1974, 6, 477-487. [all data]

Konicek, Suurkuusk, et al., 1971
Konicek, J.; Suurkuusk, J.; Wadso, I., A precise drop heat capacity calorimeter for small samples, Chemica Scripta, 1971, 1, 217-220. [all data]

Justice, 1969
Justice, B.H., Low temperature thermodynamic properties of aluminum trichloride, J. Chem. Eng. Data, 1969, 14, 4-5. [all data]

Suga and Seki, 1965
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Notes

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