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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Condensed 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:
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 | 98.2 ± 2.5 | kJ/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 | 96.7 ± 2.6 | kJ/mol | Ccb | Montgomery, Rossini, et al., 1978 | ALS |
ΔfH°solid | 100.5 ± 1.5 | kJ/mol | Ccb | Coleman and Pilcher, 1966 | ALS |
ΔfH°solid | 96.8 ± 4.0 | kJ/mol | Ccb | Mackle and O'Hare, 1963 | ALS |
ΔfH°solid | 97.2 ± 1.6 | kJ/mol | Ccb | Parks and Vaughan, 1951 | Reanalyzed by Cox and Pilcher, 1970, Original value = 96.65 kJ/mol; ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°solid | -6250. ± 20. | kJ/mol | AVG | N/A | Average of 7 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
S°solid,1 bar | 209.38 | J/mol*K | N/A | Chirico, Knipmeyer, et al., 1989 | DH |
S°solid,1 bar | 209.00 | J/mol*K | N/A | Saito, Atake, et al., 1988 | DH |
S°solid,1 bar | 205.9 | J/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 (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
285.3 | 370. | Walker, Brooks, et al., 1958 | T = 200 to 600°F.; DH |
301.2 | 422. | McEwen, March 31 1956 | T = 300 to 600°C.; DH |
300.0 | 370. | Kurbatov, 1950 | T = 98 to 255°C. Mp 70.8°C.; DH |
263.2 | 350.8 | Forrest, Brugmann, et al., 1931 | T = 350 to 620 K. Value is unsmoothed experimental datum.; DH |
259.54 | 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 (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
198.39 | 298.15 | Chirico, Knipmeyer, et al., 1989 | T = 5 to 700 K.; DH |
198.17 | 298.15 | Saito, Atake, et al., 1988 | T = 3 to 300 K.; DH |
197.7 | 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 |
190. | 300. | Wasicki, Radomska, et al., 1982 | T = 180 to 350 K. Data given graphically. Value estimated from graph.; DH |
190.8 | 298.15 | Ueberreiter and Orthmann, 1950 | T = 293 to 368 K. Equation only.; DH |
197.9 | 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 |
197.9 | 303. | Spaght, Thomas, et al., 1932 | T = 30 to 100°C.; DH |
194.1 | 294.4 | Huffman, Parks, et al., 1930 | T = 93 to 295 K. Value is unsmoothed experimental datum.; DH |
Phase change data
Go To: Top, Condensed 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
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 | 35. ± 6. | bar | 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° | 62. ± 10. | kJ/mol | AVG | N/A | Average of 7 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ΔsubH° | 82. ± 3. | kJ/mol | AVG | N/A | Average of 10 values; Individual data points |
Reduced pressure boiling point
Tboil (K) | Pressure (bar) | 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 (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
51.2 | 510. | DSC | Back, Grzyll, et al., 1996 | Based on data from 495. to 688. K.; AC |
57.4 | 400. | EB | Chirico, Knipmeyer, et al., 1989 | Based on data from 350. to 578. K.; AC |
60.3 | 360. | EB | Chirico, Knipmeyer, et al., 1989 | Based on data from 350. to 578. K.; AC |
50.4 | 500. | EB | Chirico, Knipmeyer, et al., 1989 | Based on data from 350. to 578. K.; AC |
59.6 | 363. | GS | Sakoguchi, Iwai, et al., 1989 | Based on data from 348. to 453. K.; AC |
60.4 | 363. | N/A | Sasse, N'guimbi, et al., 1989 | Based on data from 333. to 393. K.; AC |
57.3 | 405. | A | Stephenson and Malanowski, 1987 | Based on data from 390. to 563. K.; AC |
54.9 | 417. | GS | Nasir, Hwang, et al., 1980 | Based on data from 396. to 437. K.; AC |
48.0 | 647. | N/A | Glaser and Rüland, 1957 | Based on data from 528. to 766. K.; AC |
59.4 | 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 (bar)
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 | 4.35685 | 1987.623 | -71.556 | Cunningham, 1930, 2 | Coefficents calculated by NIST from author's data. |
Enthalpy of sublimation
ΔsubH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
81.520 | 298.15 | N/A | Chirico, Knipmeyer, et al., 1989 | DH |
81.8 | 383. | GS | Nass, Lenoir, et al., 1995 | Based on data from 313. to 453. K.; AC |
83.4 | 311. | EM | Sasse, N'guimbi, et al., 1989 | Based on data from 283. to 338. K.; AC |
76.0 ± 4.0 | 273. to 313. | HSA | Chickos, 1975 | AC |
80.4 ± 1.6 | 319. | TSGC | Clark, Knox, et al., 1975 | Based on data from 306. to 332. K.; AC |
75.2 | 298. to 318. | ME | Pribilová and Pouchlý, 1974 | AC |
83.6 ± 2.5 | 283. | V | Radchenko and Kitaigorodskii, 1974 | ALS |
75.81 ± 0.59 | 342.5 | V | Aihara, 1959 | ALS |
75.8 ± 0.6 | 289. | N/A | Aihara, 1955 | Based on data from 279. to 299. K.; AC |
81.6 ± 1.7 | 301. | N/A | Bradley and Cleasby, 1953 | Based on data from 288. to 314. K.; AC |
81.588 | 288.05 | V | Bradley and Cleasby, 1953, 2 | ALS |
75.1 ± 1.7 | 297. | N/A | Seki and Suzuki, 1953 | Based on data from 287. to 307. K.; AC |
68.6 ± 0.8 | 292. | QF | Wolf and Weghofer, 1938 | AC |
68.6 ± 0.8 | 295. | V | Wolf and Weghofer, 1938, 2 | ALS |
Entropy of sublimation
ΔsubS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
273.42 | 298.15 | Chirico, Knipmeyer, et al., 1989 | DH |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
18.5760 | 342.098 | N/A | Chirico, Knipmeyer, et al., 1989 | DH |
18.580 | 342.2 | N/A | O'Rourke and Mraw, 1983 | DH |
18.800 | 344.1 | N/A | Smith, 1979 | DH |
18.648 | 341.5 | N/A | Spaght, Thomas, et al., 1932 | DH |
19.7 | 342.3 | DSC | Khimeche and Dahmani, 2006 | AC |
19.27 | 344.34 | DSC | Benkhennouf, Kamel, et al., 2004 | AC |
18.66 | 341.5 | N/A | Domalski and Hearing, 1996 | AC |
18.575 | 343. | N/A | Ueberreiter and Orthmann, 1950 | DH |
18.594 | 342. | N/A | Schmidt, 1941 | DH |
18.945 | 314.3 | N/A | Eykman, 1889 | DH |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
54.300 | 342.098 | Chirico, Knipmeyer, et al., 1989 | DH |
54.3 | 342.2 | O'Rourke and Mraw, 1983 | DH |
54.6 | 344.1 | Smith, 1979 | DH |
54.6 | 341.5 | Spaght, Thomas, et al., 1932 | DH |
54.81 | 341.5 | Domalski and Hearing, 1996 | CAL |
54.2 | 343. | Ueberreiter and Orthmann, 1950 | DH |
54.4 | 342. | Schmidt, 1941 | DH |
60.3 | 314.3 | Eykman, 1889 | DH |
Enthalpy of phase transition
ΔHtrs (kJ/mol) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
0.00015 | 16.8 | crystaline, III | crystaline, II | Saito, Atake, et al., 1988 | DH |
0.00502 | 40.4 | crystaline, II | crystaline, I | Saito, Atake, et al., 1988 | Twist transition.; DH |
0.00015 | 16.8 | crystaline, III | crystaline, II | Atake, Saito, et al., 1983 | Anomalous region: 15.3 to 18.3 K.; DH |
0.00502 | 40.4 | crystaline, II | crystaline, I | Atake, Saito, et al., 1983 | Anomalous region: 30 to 47 K.; DH |
0.000293 | 11.0 | crystaline, III | crystaline, II | Ataki and Chihara, 1980 | DH |
0.00502 | 40.4 | crystaline, II | crystaline, I | Ataki and Chihara, 1980 | DH |
19.900 | 343.3 | crystaline, I | liquid | Wasicki, Radomska, et al., 1982 | DH |
Entropy of phase transition
ΔStrs (J/mol*K) | Temperature (K) | Initial Phase | Final Phase | Reference | Comment |
---|---|---|---|---|---|
0.009 | 16.8 | crystaline, III, Lock | crystaline, II, in transition | Saito, Atake, et al., 1988 | DH |
0.129 | 40.4 | crystaline, II | crystaline, I | Saito, Atake, et al., 1988 | Twist; DH |
0.009 | 16.8 | crystaline, III | crystaline, II | Atake, Saito, et al., 1983 | Anomalous; DH |
0.129 | 40.4 | crystaline, II | crystaline, I | Atake, Saito, et al., 1983 | Anomalous; DH |
0.025 | 11.0 | crystaline, III | crystaline, II | Ataki and Chihara, 1980 | DH |
0.129 | 40.4 | crystaline, II | crystaline, I | Ataki and Chihara, 1980 | DH |
58.0 | 343.3 | crystaline, I | liquid | Wasicki, Radomska, et al., 1982 | DH |
Henry's Law data
Go To: Top, Condensed phase thermochemistry data, Phase change 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 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 |
---|---|---|---|---|
1.2 | Q | N/A | missing citation give several references for the Henry's law constants but don't assign them to specific species. | |
3.6 | L | N/A | ||
3.3 | M | N/A | ||
2.5 | M | Mackay, Shiu, et al., 1979 | ||
1.2 | V | Bohon and Claussen, 1951 |
Gas phase ion energetics data
Go To: Top, Condensed 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:
MM - Michael M. Meot-Ner (Mautner)
LLK - Sharon G. Lias, Rhoda D. Levin, and Sherif A. Kafafi
RDSH - Henry M. Rosenstock, Keith Draxl, Bruce W. Steiner, and John T. Herron
B - John E. Bartmess
View reactions leading to C12H10+ (ion structure unspecified)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
IE (evaluated) | 8.16 ± 0.13 | eV | N/A | N/A | L |
Quantity | Value | Units | Method | Reference | Comment |
Proton affinity (review) | 813.6 | kJ/mol | N/A | Hunter and Lias, 1998 | HL |
Quantity | Value | Units | Method | Reference | Comment |
Gas basicity | 782.9 | kJ/mol | N/A | Hunter and Lias, 1998 | HL |
Electron affinity determinations
EA (eV) | Method | Reference | Comment |
---|---|---|---|
<0.130 ± 0.035 | ECD | Wojnarovits and Foldiak, 1981 | EA is an upper limit: Chen and Wentworth, 1989. G3MP2B3 calculations indicate an EA of ca. -0.02 eV, anion unbound.; B |
Proton affinity at 298K
Proton affinity (kJ/mol) | Reference | Comment |
---|---|---|
808.8 | Aue, Guidoni, et al., 2000 | Experimental literature data re-evaluated by the authors using ab initio protonation entropies; MM |
Gas basicity at 298K
Gas basicity (review) (kJ/mol) | Reference | Comment |
---|---|---|
780.7 | Aue, Guidoni, et al., 2000 | Experimental literature data re-evaluated by the authors using ab initio protonation entropies; MM |
Ionization energy determinations
IE (eV) | Method | Reference | Comment |
---|---|---|---|
8.80 ± 0.05 | EI | Loudon and Mazengo, 1974 | LLK |
8.9 | EI | Koppel, Schwarz, et al., 1974 | LLK |
7.95 ± 0.02 | PE | Maier and Turner, 1972 | LLK |
8.23 ± 0.01 | PE | Dewar, Haselbach, et al., 1970 | RDSH |
8.20 ± 0.05 | PE | Eland and Danby, 1968 | RDSH |
8.46 | CTS | Slifkin and Allison, 1967 | RDSH |
8.22 ± 0.15 | EI | Eland, Shepherd, et al., 1966 | RDSH |
8.27 ± 0.01 | PI | Watanabe, Nakayama, et al., 1962 | RDSH |
8.64 | CTS | Kinoshita, 1962 | RDSH |
8.35 | CTS | Briegleb, Czekalla, et al., 1961 | RDSH |
8.4 | CTS | Briegleb and Czekalla, 1959 | RDSH |
8.39 | PE | Akiyama, Li, et al., 1979 | Vertical value; LLK |
8.34 | PE | Ruscic, Kovac, et al., 1978 | Vertical value; LLK |
Appearance energy determinations
Ion | AE (eV) | Other Products | Method | Reference | Comment |
---|---|---|---|---|---|
C6H4+ | 18.1 ± 0.3 | ? | EI | Natalis and Franklin, 1965 | RDSH |
C6H5+ | 18.2 ± 0.5 | ? | EI | Natalis and Franklin, 1965 | RDSH |
C7H5+ | 20.9 ± 0.2 | ? | EI | Natalis and Franklin, 1965 | RDSH |
C8H6+ | 18.10 ± 0.05 | ? | EI | Natalis and Franklin, 1965 | RDSH |
C9H7+ | 16.08 ± 0.05 | ? | EI | Natalis and Franklin, 1965 | RDSH |
C10H8+ | 14.81 ± 0.05 | ? | EI | Natalis and Franklin, 1965 | RDSH |
C11H7+ | 14.8 ± 0.2 | CH3 | EI | Loudon and Mazengo, 1974 | LLK |
C12H8+ | 16.89 ± 0.08 | ? | EI | Natalis and Franklin, 1965 | RDSH |
C12H9+ | 13.6 ± 0.2 | H | EI | Loudon and Mazengo, 1974 | LLK |
C12H9+ | 14.36 | H | EI | Natalis and Franklin, 1965 | RDSH |
C12H82+ | 22.0 ± 1.0 | ? | EI | Natalis and Franklin, 1965 | RDSH |
References
Go To: Top, Condensed 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.
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]
Parks and Huffman, 1931
Parks, G.S.; Huffman, H.M.,
Some fusion and transition data for hydrocarbons,
Ind. Eng. Chem., 1931, 23, 1138-9. [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]
Ellard and Yanko, 1963
Ellard, J.A.; Yanko, W.H.,
, U. S. A. E. C. Rep. IDO-11008, 1963. [all data]
Reiter, 1963
Reiter, R.W.,
, NASA Doc. N63-19495 1963 1963, 1963. [all data]
Mandel and Ewbank, 1960
Mandel, H.; Ewbank, N.,
, Atomics International NAA-S-R-5129 1960, 1960. [all data]
Weast and Grasselli, 1989
CRC Handbook of Data on Organic Compounds, 2nd Editon, Weast,R.C and Grasselli, J.G., ed(s)., CRC Press, Inc., Boca Raton, FL, 1989, 1. [all data]
Buckingham and Donaghy, 1982
Buckingham, J.; Donaghy, S.M.,
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Notes
Go To: Top, Condensed phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics data, References
- Symbols used in this document:
AE Appearance energy Cp,liquid Constant pressure heat capacity of liquid Cp,solid Constant pressure heat capacity of solid EA Electron affinity IE (evaluated) Recommended ionization energy Pc Critical pressure 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 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°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 ρc Critical density - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
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