Biphenyl
- Formula: C12H10
- Molecular weight: 154.2078
- IUPAC Standard InChIKey: ZUOUZKKEUPVFJK-UHFFFAOYSA-N
- CAS Registry Number: 92-52-4
- 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: 1,1'-Biphenyl; Bibenzene; Diphenyl; Phenylbenzene; 1,1'-Diphenyl; Lemonene; Phenador-X; PhPh; Xenene; Carolid AL; Tetrosin LY; NSC 14916; 1,1-Biphenyl
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Gas phase thermochemistry data
Go To: Top, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, IR 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 | 43.1 ± 0.7 | kcal/mol | AVG | N/A | Average of 6 values; Individual data points |
Constant pressure heat capacity of gas
Cp,gas (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
12.03 | 50. | Dorofeeva O.V., 1997 | None of the statistically calculated values of S(T) known from literature [ Trevissoi C., 1955, Katon J.E., 1959, Aleman H., 1973, Thermodynamics Research Center, 1997] is in full accord with experimental data (see also discussion in [ Chirico R.D., 1989]). Recommended values agree with experimental values within their uncertainties except for temperature range 340-460 K where discrepancies amount to 0.4-0.6 J/mol*K.; GT |
15.49 | 100. | ||
20.14 | 150. | ||
26.030 | 200. | ||
36.202 | 273.15 | ||
39.84 ± 0.24 | 298.15 | ||
40.105 | 300. | ||
53.903 | 400. | ||
65.397 | 500. | ||
74.517 | 600. | ||
81.773 | 700. | ||
87.655 | 800. | ||
92.512 | 900. | ||
96.573 | 1000. | ||
100.00 | 1100. | ||
102.93 | 1200. | ||
105.43 | 1300. | ||
107.57 | 1400. | ||
109.43 | 1500. |
Condensed phase thermochemistry data
Go To: Top, Gas phase thermochemistry data, Phase change data, Reaction thermochemistry data, IR 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 |
---|---|---|---|---|---|
ΔfH°solid | 23.5 ± 0.60 | kcal/mol | Review | Roux, Temprado, et al., 2008 | There are sufficient high-quality literature values to make a good evaluation with a high degree of confidence. In general, the evaluated uncertainty limits are on the order of (0.5 to 2.5) kJ/mol.; DRB |
ΔfH°solid | 23.12 ± 0.62 | kcal/mol | Ccb | Montgomery, Rossini, et al., 1978 | ALS |
ΔfH°solid | 24.02 ± 0.36 | kcal/mol | Ccb | Coleman and Pilcher, 1966 | ALS |
ΔfH°solid | 23.14 ± 0.96 | kcal/mol | Ccb | Mackle and O'Hare, 1963 | ALS |
ΔfH°solid | 23.24 ± 0.39 | kcal/mol | Ccb | Parks and Vaughan, 1951 | Reanalyzed by Cox and Pilcher, 1970, Original value = 23.10 kcal/mol; ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°solid | -1494. ± 5. | kcal/mol | AVG | N/A | Average of 7 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
S°solid,1 bar | 50.043 | cal/mol*K | N/A | Chirico, Knipmeyer, et al., 1989 | DH |
S°solid,1 bar | 49.952 | cal/mol*K | N/A | Saito, Atake, et al., 1988 | DH |
S°solid,1 bar | 49.21 | cal/mol*K | N/A | Huffman, Parks, et al., 1930 | Extrapolation below 90 K, 65.4 J/mol*K.; DH |
Constant pressure heat capacity of liquid
Cp,liquid (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
68.19 | 370. | Walker, Brooks, et al., 1958 | T = 200 to 600°F.; DH |
71.99 | 422. | McEwen, March 31 1956 | T = 300 to 600°C.; DH |
71.70 | 370. | Kurbatov, 1950 | T = 98 to 255°C. Mp 70.8°C.; DH |
62.91 | 350.8 | Forrest, Brugmann, et al., 1931 | T = 350 to 620 K. Value is unsmoothed experimental datum.; DH |
62.032 | 298. | Newton, Kaura, et al., 1931 | T = 100 to 300°C, equation only, in t°C. Cp(liq) = 0.388 + 0.00057t cal/g*K.; DH |
Constant pressure heat capacity of solid
Cp,solid (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
47.416 | 298.15 | Chirico, Knipmeyer, et al., 1989 | T = 5 to 700 K.; DH |
47.364 | 298.15 | Saito, Atake, et al., 1988 | T = 3 to 300 K.; DH |
47.25 | 298.15 | O'Rourke and Mraw, 1983 | T = 220 to 475 K. Cp = 0.7143 (T/K) - 15.3 (220 to 342.2 K) J/mol*K.; DH |
45.4 | 300. | Wasicki, Radomska, et al., 1982 | T = 180 to 350 K. Data given graphically. Value estimated from graph.; DH |
45.60 | 298.15 | Ueberreiter and Orthmann, 1950 | T = 293 to 368 K. Equation only.; DH |
47.30 | 298.1 | Schmidt, 1941 | T = 20 to 200°C, equations only, in t°C. Cp(c) = 0.2745 + 0.001235t cal/g*K (20 to 69°C); Cp(liq) = 0.3917 + 0.0005206t cal/g*K (69 to 200°C).; DH |
47.30 | 303. | Spaght, Thomas, et al., 1932 | T = 30 to 100°C.; DH |
46.39 | 294.4 | Huffman, Parks, et al., 1930 | T = 93 to 295 K. Value is unsmoothed experimental datum.; DH |
Phase change data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Reaction thermochemistry data, IR 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
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
DRB - Donald R. Burgess, Jr.
DH - Eugene S. Domalski and Elizabeth D. Hearing
CAL - James S. Chickos, William E. Acree, Jr., Joel F. Liebman, Students of Chem 202 (Introduction to the Literature of Chemistry), University of Missouri -- St. Louis
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 527. ± 2. | K | AVG | N/A | Average of 40 out of 42 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 343. ± 1. | K | AVG | N/A | Average of 285 out of 294 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 342.090 | K | N/A | Chirico, Knipmeyer, et al., 1989, 2 | Uncertainty assigned by TRC = 0.01 K; TRC |
Ttriple | 341.8 | K | N/A | Parks and Huffman, 1931 | Uncertainty assigned by TRC = 0.3 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 780. ± 20. | K | AVG | N/A | Average of 7 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 34. ± 6. | atm | AVG | N/A | Average of 8 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Vc | 0.497 | l/mol | N/A | Tsonopoulos and Ambrose, 1995 | |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 2.0 ± 0.1 | mol/l | N/A | Tsonopoulos and Ambrose, 1995 | |
ρc | 2.01 | mol/l | N/A | Ellard and Yanko, 1963 | Uncertainty assigned by TRC = 0.065 mol/l; TRC |
ρc | 2.09 | mol/l | N/A | Reiter, 1963 | Uncertainty assigned by TRC = 0.065 mol/l; TRC |
ρc | 1.99 | mol/l | N/A | Mandel and Ewbank, 1960 | Uncertainty assigned by TRC = 0.097 mol/l; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 15. ± 3. | kcal/mol | AVG | N/A | Average of 7 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ΔsubH° | 19.5 ± 0.7 | kcal/mol | AVG | N/A | Average of 10 values; Individual data points |
Reduced pressure boiling point
Tboil (K) | Pressure (atm) | Reference | Comment |
---|---|---|---|
418.2 | 0.029 | Weast and Grasselli, 1989 | BS |
418. | 0.029 | Buckingham and Donaghy, 1982 | BS |
343. to 351. | 0.0003 | Buckingham and Donaghy, 1982 | BS |
Enthalpy of vaporization
ΔvapH (kcal/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
12.2 | 510. | DSC | Back, Grzyll, et al., 1996 | Based on data from 495. to 688. K.; AC |
13.7 | 400. | EB | Chirico, Knipmeyer, et al., 1989 | Based on data from 350. to 578. K.; AC |
14.4 | 360. | EB | Chirico, Knipmeyer, et al., 1989 | Based on data from 350. to 578. K.; AC |
12.0 | 500. | EB | Chirico, Knipmeyer, et al., 1989 | Based on data from 350. to 578. K.; AC |
14.2 | 363. | GS | Sakoguchi, Iwai, et al., 1989 | Based on data from 348. to 453. K.; AC |
14.4 | 363. | N/A | Sasse, N'guimbi, et al., 1989 | Based on data from 333. to 393. K.; AC |
13.7 | 405. | A | Stephenson and Malanowski, 1987 | Based on data from 390. to 563. K.; AC |
13.1 | 417. | GS | Nasir, Hwang, et al., 1980 | Based on data from 396. to 437. K.; AC |
11.5 | 647. | N/A | Glaser and Rüland, 1957 | Based on data from 528. to 766. K.; AC |
14.2 | 357. | N/A | Cunningham, 1930 | Based on data from 342. to 544. K. See also Boublik, Fried, et al., 1984.; AC |
Antoine Equation Parameters
log10(P) = A − (B / (T + C))
P = vapor pressure (atm)
T = temperature (K)
View plot Requires a JavaScript / HTML 5 canvas capable browser.
Temperature (K) | A | B | C | Reference | Comment |
---|---|---|---|---|---|
342.3 to 544.3 | 4.35114 | 1987.623 | -71.556 | Cunningham, 1930, 2 | Coefficents calculated by NIST from author's data. |
Enthalpy of sublimation
ΔsubH (kcal/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
19.484 | 298.15 | N/A | Chirico, Knipmeyer, et al., 1989 | DH |
19.6 | 383. | GS | Nass, Lenoir, et al., 1995 | Based on data from 313. to 453. K.; AC |
19.9 | 311. | EM | Sasse, N'guimbi, et al., 1989 | Based on data from 283. to 338. K.; AC |
18.2 ± 0.96 | 273. to 313. | HSA | Chickos, 1975 | AC |
19.2 ± 0.38 | 319. | TSGC | Clark, Knox, et al., 1975 | Based on data from 306. to 332. K.; AC |
18.0 | 298. to 318. | ME | Pribilová and Pouchlý, 1974 | AC |
19.98 ± 0.59 | 283. | V | Radchenko and Kitaigorodskii, 1974 | ALS |
18.12 ± 0.14 | 342.5 | V | Aihara, 1959 | ALS |
18.1 ± 0.1 | 289. | N/A | Aihara, 1955 | Based on data from 279. to 299. K.; AC |
19.5 ± 0.41 | 301. | N/A | Bradley and Cleasby, 1953 | Based on data from 288. to 314. K.; AC |
19.500 | 288.05 | V | Bradley and Cleasby, 1953, 2 | ALS |
17.9 ± 0.41 | 297. | N/A | Seki and Suzuki, 1953 | Based on data from 287. to 307. K.; AC |
16.4 ± 0.2 | 292. | QF | Wolf and Weghofer, 1938 | AC |
16.4 ± 0.2 | 295. | V | Wolf and Weghofer, 1938, 2 | ALS |
Entropy of sublimation
ΔsubS (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
65.349 | 298.15 | Chirico, Knipmeyer, et al., 1989 | DH |
Enthalpy of fusion
ΔfusH (kcal/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
4.43977 | 342.098 | N/A | Chirico, Knipmeyer, et al., 1989 | DH |
4.4407 | 342.2 | N/A | O'Rourke and Mraw, 1983 | DH |
4.4933 | 344.1 | N/A | Smith, 1979 | DH |
4.4570 | 341.5 | N/A | Spaght, Thomas, et al., 1932 | DH |
4.71 | 342.3 | DSC | Khimeche and Dahmani, 2006 | AC |
4.606 | 344.34 | DSC | Benkhennouf, Kamel, et al., 2004 | AC |
4.460 | 341.5 | N/A | Domalski and Hearing, 1996 | AC |
4.4395 | 343. | N/A | Ueberreiter and Orthmann, 1950 | DH |
4.4441 | 342. | N/A | Schmidt, 1941 | DH |
4.5280 | 314.3 | N/A | Eykman, 1889 | DH |
Entropy of fusion
ΔfusS (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
12.978 | 342.098 | Chirico, Knipmeyer, et al., 1989 | DH |
13.0 | 342.2 | O'Rourke and Mraw, 1983 | DH |
13.0 | 344.1 | Smith, 1979 | DH |
13.0 | 341.5 | Spaght, Thomas, et al., 1932 | DH |
13.10 | 341.5 | Domalski and Hearing, 1996 | CAL |
13.0 | 343. | Ueberreiter and Orthmann, 1950 | DH |
13.0 | 342. | Schmidt, 1941 | DH |
14.4 | 314.3 | Eykman, 1889 | DH |
Enthalpy of phase transition
ΔHtrs (kcal/mol) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
0.000036 | 16.8 | crystaline, III | crystaline, II | Saito, Atake, et al., 1988 | DH |
0.00120 | 40.4 | crystaline, II | crystaline, I | Saito, Atake, et al., 1988 | Twist transition.; DH |
0.000036 | 16.8 | crystaline, III | crystaline, II | Atake, Saito, et al., 1983 | Anomalous region: 15.3 to 18.3 K.; DH |
0.00120 | 40.4 | crystaline, II | crystaline, I | Atake, Saito, et al., 1983 | Anomalous region: 30 to 47 K.; DH |
0.000070 | 11.0 | crystaline, III | crystaline, II | Ataki and Chihara, 1980 | DH |
0.00120 | 40.4 | crystaline, II | crystaline, I | Ataki and Chihara, 1980 | DH |
4.7562 | 343.3 | crystaline, I | liquid | Wasicki, Radomska, et al., 1982 | DH |
Entropy of phase transition
ΔStrs (cal/mol*K) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
0.002 | 16.8 | crystaline, III, Lock | crystaline, II, in transition | Saito, Atake, et al., 1988 | DH |
0.0308 | 40.4 | crystaline, II | crystaline, I | Saito, Atake, et al., 1988 | Twist; DH |
0.002 | 16.8 | crystaline, III | crystaline, II | Atake, Saito, et al., 1983 | Anomalous; DH |
0.0308 | 40.4 | crystaline, II | crystaline, I | Atake, Saito, et al., 1983 | Anomalous; DH |
0.0060 | 11.0 | crystaline, III | crystaline, II | Ataki and Chihara, 1980 | DH |
0.0308 | 40.4 | crystaline, II | crystaline, I | Ataki and Chihara, 1980 | DH |
13.9 | 343.3 | crystaline, I | liquid | Wasicki, Radomska, et al., 1982 | DH |
Reaction thermochemistry data
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, IR 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:
M - Michael M. Meot-Ner (Mautner) and Sharon G. Lias
MS - José A. Martinho Simões
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
By formula: C10H8+ + C12H10 = (C10H8+ • C12H10)
Bond type: Charge transfer bond (positive ion)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 13.5 | kcal/mol | PHPMS | Meot-Ner (Mautner), 1980 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 28. | cal/mol*K | N/A | Meot-Ner (Mautner), 1980 | gas phase; Entropy change calculated or estimated; M |
Free energy of reaction
ΔrG° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
5.2 | 297. | PHPMS | Meot-Ner (Mautner), 1980 | gas phase; Entropy change calculated or estimated; M |
By formula: C12H8+ + C12H10 = (C12H8+ • C12H10)
Bond type: Charge transfer bond (positive ion)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 13.4 | kcal/mol | PHPMS | Meot-Ner (Mautner), 1980 | gas phase; Entropy change calculated or estimated; M |
Quantity | Value | Units | Method | Reference | Comment |
ΔrS° | 28. | cal/mol*K | N/A | Meot-Ner (Mautner), 1980 | gas phase; Entropy change calculated or estimated; M |
Free energy of reaction
ΔrG° (kcal/mol) | T (K) | Method | Reference | Comment |
---|---|---|---|---|
5.5 | 279. | PHPMS | Meot-Ner (Mautner), 1980 | gas phase; Entropy change calculated or estimated; M |
C17H24F3N3O3RuS (solution) + (solution) = C23H25F3O3RuS (solution) + 3 (solution)
By formula: C17H24F3N3O3RuS (solution) + C12H10 (solution) = C23H25F3O3RuS (solution) + 3C2H3N (solution)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -3.61 ± 0.1 | kcal/mol | RSC | Nolan, Martin, et al., 1992 | solvent: Tetrahydrofuran; MS |
By formula: 3H2 + C12H10 = C12H16
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | -54. | kcal/mol | Eqk | Frye, 1962 | liquid phase; ALS |
IR Spectrum
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, References, Notes
Data compiled by: Coblentz Society, Inc.
- SOLUTION (10% CCl4 FOR 4000-1340, 10% CCl4 FOR 430-200, 10% CS2 FOR 1340-430 CM-1); BECKMAN IR-12 (GRATING); DIGITIZED BY COBLENTZ SOCIETY (BATCH I) FROM HARD COPY; 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
References
Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, IR Spectrum, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Dorofeeva O.V., 1997
Dorofeeva O.V.,
Unpublished results. Thermocenter of Russian Academy of Science, Moscow, 1997. [all data]
Trevissoi C., 1955
Trevissoi C.,
Specific heat and entropy of biphenyl,
Ann. Chim. (Rome), 1955, 45, 943-959. [all data]
Katon J.E., 1959
Katon J.E.,
The vibrational spectra and geometrical configuration of biphenyl,
Spectrochim. Acta, 1959, 15, 627-650. [all data]
Aleman H., 1973
Aleman H.,
Thermodynamic functions for biphenyl and the 4,4'-dihalogenobiphenyls,
Thermochim. Acta, 1973, 7, 69-73. [all data]
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]
Chirico R.D., 1989
Chirico R.D.,
The thermodynamic properties of biphenyl,
J. Chem. Thermodyn., 1989, 21, 1307-1331. [all data]
Roux, Temprado, et al., 2008
Roux, M.V.; Temprado, M.; Chickos, J.S.; Nagano, Y.,
Critically Evaluated Thermochemical Properties of Polycyclic Aromatic Hydrocarbons,
J. Phys. Chem. Ref. Data, 2008, 37, 4, 1855-1996. [all data]
Montgomery, Rossini, et al., 1978
Montgomery, R.L.; Rossini, F.D.; Mansson, M.,
Enthalpies of combustion, vaporization, and formation of phenylbenzene, cyclohexylbenzene, and cyclohexylcyclohexane; enthalpy of hydrogenation of certain aromatic systems,
J. Chem. Eng. Data, 1978, 23, 125-129. [all data]
Coleman and Pilcher, 1966
Coleman, D.J.; Pilcher, G.,
Heats of combustion of biphenyl, bibenzyl, naphthalene, anthracene, and phenanthrene,
Trans. Faraday Soc., 1966, 62, 821-827. [all data]
Mackle and O'Hare, 1963
Mackle, H.; O'Hare, P.A.G.,
A high-precision aneroid semi-micro combustion calorimeter,
Trans. Faraday Soc., 1963, 59, 2693-2701. [all data]
Parks and Vaughan, 1951
Parks, G.S.; Vaughan, L.M.,
The heat of combustion of biphenyl,
J. Am. Chem. Soc., 1951, 73, 2380-2381. [all data]
Cox and Pilcher, 1970
Cox, J.D.; Pilcher, G.,
Thermochemistry of Organic and Organometallic Compounds, Academic Press, New York, 1970, 1-636. [all data]
Chirico, Knipmeyer, et al., 1989
Chirico, R.D.; Knipmeyer, S.E.; Nguyen, A.; Steele, W.V.,
The thermodynamic properties of biphenyl,
J. Chem. Thermodyn., 1989, 21, 1307-1331. [all data]
Saito, Atake, et al., 1988
Saito, K.; Atake, T.; Chihara, H.,
Incommensurate phase transitions and anomalous lattice heat capacities of biphenyl,
Bull. Chem. Soc. Japan, 1988, 61, 679-688. [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]
Walker, Brooks, et al., 1958
Walker, B.E., Jr.; Brooks, M.S.; Ewing, C.T.; Miller, R.R.,
Specific heat of biphenyl and other polyphenyls. Correlation of specific heat data for phenyl type compounds,
J. Chem. Eng. Data, 1958, 3, 280-282. [all data]
McEwen, March 31 1956
McEwen, M.,
Preliminary engineering study of organic nuclear reactor coolant-moderators Monsanto Chemical Co, March 31 1956. [all data]
Kurbatov, 1950
Kurbatov, V.Ya.,
Specific heats of liquids. III. Specific heat of hydrocarbons with several noncondensed rings,
Zhur. Obshch. Khim., 1950, 20, 1139-1144. [all data]
Forrest, Brugmann, et al., 1931
Forrest, H.O.; Brugmann, E.W.; Cummings, L.W.T.,
The specific heat of diphenyl,
Ind. Eng. Chem., 1931, 23, 37-39. [all data]
Newton, Kaura, et al., 1931
Newton, R.F.; Kaura, B.D.; DeVries, T.,
The specific heat of liquid diphenyl,
Ind. Eng. Chem., 1931, 23, 35-37. [all data]
O'Rourke and Mraw, 1983
O'Rourke, D.F.; Mraw, S.C.,
Heat capacities and enthalpies of fusion of dibenzothiophene (220 to 560 K) and of biphenyl, cyclohexylbenzene, and cyclohexylcyclohexane (220 to 475 K). Enthalpies and temperatures of three transitions in solid cyclohexylcyclohexane,
J. Chem. Thermodynam., 1983, 15, 489-502. [all data]
Wasicki, Radomska, et al., 1982
Wasicki, J.; Radomska, M.; Radomski, R.,
Heat capacities of diphenyl, p-terphenyl and p-quaterphenyl from 180 K to their melting points,
J. Therm. Anal., 1982, 25, 509-514. [all data]
Ueberreiter and Orthmann, 1950
Ueberreiter, K.; Orthmann, H.-J.,
Specifische Wärme, spezifisches Volumen, Temperatur- und Wärme-leittähigkeit einiger disubstituierter Benzole und polycyclischer Systeme,
Z. Natursforsch. 5a, 1950, 101-108. [all data]
Schmidt, 1941
Schmidt, W.R.,
Thesis Washington University (St. Louis), 1941. [all data]
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,
J. Phys. Chem., 1932, 36, 882-888. [all data]
Chirico, Knipmeyer, et al., 1989, 2
Chirico, R.D.; Knipmeyer, S.E.; Nguyen, A.; Steele, W.V.,
The thermodynamic properties of biphenyl,
J. Chem. Thermodyn., 1989, 21, 1307-31. [all data]
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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°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 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 ρc Critical density - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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