p-Xylene
- Formula: C8H10
- Molecular weight: 106.1650
- IUPAC Standard InChIKey: URLKBWYHVLBVBO-UHFFFAOYSA-N
- CAS Registry Number: 106-42-3
- 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: Benzene, 1,4-dimethyl-; p-Dimethylbenzene; p-Xylol; 1,4-Dimethylbenzene; 1,4-Xylene; p-Methyltoluene; para-Xylene; Chromar; Scintillar; 4-Methyltoluene; NSC 72419; UN 1307; 1,4-dimethyl-benzene ( p-xylene)
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Gas phase thermochemistry data
Go To: Top, Condensed phase thermochemistry data, 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:
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 | 4.29 ± 0.24 | kcal/mol | Ccb | Prosen, Johnson, et al., 1946 | ALS |
Constant pressure heat capacity of gas
Cp,gas (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
10.68 | 50. | Chao J., 1986 | Among the known statistically calculated values [ Pitzer K.S., 1943, Taylor W.J., 1946, Draeger J.A., 1981, Draeger, 1985], the recommended S(T) and Cp(T) values are in best agreement with the experimental data. With the exception of [ Draeger J.A., 1981], all calculations agree within 1.2 J/mol*K for S(T) and Cp(T). Discrepancy with Cp(1000 K) calculated by [ Draeger J.A., 1981] amounts to 4.7 J/mol*K.; GT |
13.14 | 100. | ||
16.68 | 150. | ||
20.79 | 200. | ||
27.65 | 273.15 | ||
30.11 | 298.15 | ||
30.31 | 300. | ||
40.01 | 400. | ||
48.59 | 500. | ||
55.74 | 600. | ||
61.69 | 700. | ||
66.66 | 800. | ||
70.84 | 900. | ||
74.43 | 1000. | ||
77.49 | 1100. | ||
80.11 | 1200. | ||
82.39 | 1300. | ||
84.32 | 1400. | ||
86.02 | 1500. |
Constant pressure heat capacity of gas
Cp,gas (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
39.00 ± 0.40 | 393. | Hossenlopp I.A., 1981 | Please also see Pitzer K.S., 1943, Taylor W.J., 1946.; GT |
39.799 ± 0.079 | 398.15 | ||
42.022 ± 0.084 | 423.15 | ||
42.60 ± 0.40 | 428. | ||
44.312 ± 0.088 | 448.15 | ||
45.20 ± 0.40 | 463. | ||
46.408 ± 0.093 | 473.15 | ||
48.499 ± 0.098 | 498.15 | ||
50.45 ± 0.10 | 523.15 |
Condensed 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 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 |
---|---|---|---|---|---|
ΔfH°liquid | -5.84 ± 0.24 | kcal/mol | Ccb | Prosen, Johnson, et al., 1946 | ALS |
Quantity | Value | Units | Method | Reference | Comment |
ΔcH°liquid | -1087.82 ± 0.12 | kcal/mol | Cm | Coops, Mulder, et al., 1946 | Reanalyzed by Cox and Pilcher, 1970, Original value = -1086.94 ± 0.12 kcal/mol; Corresponding ΔfHºliquid = -6.16 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -1088.16 ± 0.22 | kcal/mol | Ccb | Prosen, Johnson, et al., 1946 | Corresponding ΔfHºliquid = -5.82 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -1087.9 | kcal/mol | Ccb | Richards and Barry, 1915 | At 291 K; Corresponding ΔfHºliquid = -6.09 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS |
ΔcH°liquid | -1091.3 | kcal/mol | Ccb | Richards and Jesse, 1910 | At 293 K; Corresponding ΔfHºliquid = -2.70 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS |
Quantity | Value | Units | Method | Reference | Comment |
S°liquid | 59.0712 | cal/mol*K | N/A | Messerly, Finke, et al., 1988 | DH |
S°liquid | 58.200 | cal/mol*K | N/A | Pitzer and Scott, 1943 | DH |
S°liquid | 60.49 | cal/mol*K | N/A | Huffman, Parks, et al., 1930 | Extrapolation below 90 K, 65.19 J/mol*K.; DH |
Constant pressure heat capacity of liquid
Cp,liquid (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
43.5514 | 298.15 | Messerly, Finke, et al., 1988 | T = 10 to 400 K.; DH |
43.893 | 298.15 | Tardajos, Aicart, et al., 1986 | DH |
43.4840 | 298.15 | Fortier and Benson, 1979 | DH |
43.48 | 298.15 | Ott, Goates, et al., 1979 | T = 288.15 to 328.15 K.; DH |
43.4498 | 298.15 | Fortier and Benson, 1977 | DH |
43.391 | 298.15 | Wilhelm, Grolier, et al., 1977 | DH |
43.43 | 298.15 | Hyder Khan and Subrahmanyam, 1971 | T = 298; 313 K.; DH |
47.49 | 336. | Swietoslawski and Zielenkiewicz, 1958 | Mean value 21 to 106 C.; DH |
43.40 | 298. | Corruccini and Ginnings, 1947 | T = 273 to 573 K.; DH |
44.19 | 298. | Kurbatov, 1947 | T = 15 to 132 C, mean Cp, three temperatures.; DH |
43.920 | 298.15 | Pitzer and Scott, 1943 | T = 14 to 360 K.; DH |
43.09 | 299.0 | Huffman, Parks, et al., 1930 | T = 92 to 299 K. Value is unsmoothed experimental datum.; DH |
42.21 | 303. | Willams and Daniels, 1924 | T = 303 to 348 K. Equation only.; 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:
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, Chris Muzny director
BS - Robert L. Brown and Stephen E. Stein
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
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 411.4 ± 0.5 | K | AVG | N/A | Average of 59 out of 65 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 286.3 ± 0.2 | K | AVG | N/A | Average of 18 out of 21 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 286.400 | K | N/A | Messerly, Finke, et al., 1988, 2 | Uncertainty assigned by TRC = 0.01 K; TRC |
Ttriple | 286.3 | K | N/A | Huffman, Parks, et al., 1930, 2 | Uncertainty assigned by TRC = 0.3 K; TRC |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 617. ± 3. | K | AVG | N/A | Average of 12 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 34. ± 2. | atm | AVG | N/A | Average of 6 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Vc | 0.378 | l/mol | N/A | Tsonopoulos and Ambrose, 1995 | |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 2.65 ± 0.02 | mol/l | N/A | Tsonopoulos and Ambrose, 1995 | |
ρc | 2.661 | mol/l | N/A | Akhundov and Imanov, 1970 | Uncertainty assigned by TRC = 0.05 mol/l; TRC |
ρc | 2.644 | mol/l | N/A | Simon, 1957 | Uncertainty assigned by TRC = 0.04 mol/l; TRC |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 10. ± 1. | kcal/mol | AVG | N/A | Average of 14 values; Individual data points |
Enthalpy of vaporization
ΔvapH (kcal/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
8.525 | 411.5 | N/A | Majer and Svoboda, 1985 | |
9.63 | 353. | N/A | Hossenlopp and Archer, 1988 | AC |
8.91 | 426. | A | Stephenson and Malanowski, 1987 | Based on data from 411. to 463. K.; AC |
8.63 | 475. | A | Stephenson and Malanowski, 1987 | Based on data from 460. to 553. K.; AC |
8.65 | 566. | A | Stephenson and Malanowski, 1987 | Based on data from 551. to 616. K.; AC |
10.1 | 301. | IP,EB | Stephenson and Malanowski, 1987 | Based on data from 286. to 453. K. See also Osborn and Douslin, 1974.; AC |
8.60 ± 0.02 | 411. | C | Natarajan and Viswanath, 1985 | AC |
8.25 ± 0.02 | 436. | C | Natarajan and Viswanath, 1985 | AC |
7.29 ± 0.02 | 484. | C | Natarajan and Viswanath, 1985 | AC |
5.90 ± 0.02 | 540. | C | Natarajan and Viswanath, 1985 | AC |
8.91 | 395. | N/A | Castellari, Francesconi, et al., 1982 | Based on data from 380. to 410. K.; AC |
9.94 | 318. | N/A | Gaw and Swinton, 1968 | Based on data from 303. to 343. K.; AC |
9.58 | 347. | MM | Willingham, Taylor, et al., 1945 | Based on data from 332. to 413. K. See also Forziati, Norris, et al., 1949.; AC |
Enthalpy of vaporization
ΔvapH =
A exp(-βTr) (1 − Tr)β
ΔvapH =
Enthalpy of vaporization (at saturation pressure)
(kcal/mol)
Tr = reduced temperature (T / Tc)
View plot Requires a JavaScript / HTML 5 canvas capable browser.
Temperature (K) | A (kcal/mol) | β | Tc (K) | Reference | Comment |
---|---|---|---|---|---|
298. to 440. | 13.91 | 0.2768 | 616.2 | Majer and Svoboda, 1985 |
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 |
---|---|---|---|---|---|
286.43 to 452.38 | 4.13982 | 1474.403 | -55.377 | Osborn and Douslin, 1974 | Coefficents calculated by NIST from author's data. |
420.00 to 600.00 | 4.50373 | 1788.91 | -13.902 | Ambrose, Broderick, et al., 1967 | Coefficents calculated by NIST from author's data. |
331.44 to 412.44 | 4.10567 | 1450.688 | -58.16 | Williamham, Taylor, et al., 1945 | |
298. to 333. | 4.44318 | 1644.214 | -40.229 | Pitzer and Scott, 1943 | Coefficents calculated by NIST from author's data. |
Enthalpy of sublimation
ΔsubH (kcal/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
14.2 | 271. | N/A | Stephenson and Malanowski, 1987 | Based on data from 247. to 286. K. See also Osborn and Douslin, 1974.; AC |
14.5 | 286. | B | Hessler and Lichtenstein, 1986 | AC |
Enthalpy of fusion
ΔfusH (kcal/mol) | Temperature (K) | Reference | Comment |
---|---|---|---|
4.091172 | 286.405 | Messerly, Finke, et al., 1988 | DH |
4.0870 | 286.3 | Corruccini and Ginnings, 1947 | DH |
4.0901 | 286.39 | Pitzer and Scott, 1943 | DH |
4.089 | 286.3 | Domalski and Hearing, 1996 | AC |
4.0471 | 286.3 | Huffman, Parks, et al., 1930 | DH |
Entropy of fusion
ΔfusS (cal/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
14.29 | 286.405 | Messerly, Finke, et al., 1988 | DH |
14.28 | 286.3 | Corruccini and Ginnings, 1947 | DH |
14.28 | 286.39 | Pitzer and Scott, 1943 | DH |
14.13 | 286.3 | Huffman, Parks, et al., 1930 | DH |
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) = 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 |
---|---|---|---|---|
0.13 | 3800. | L | N/A | |
0.17 | 4500. | M | N/A | |
0.12 | 3000. | X | N/A | |
0.16 | Q | N/A | missing citation give several references for the Henry's law constants but don't assign them to specific species. | |
0.12 | 5300. | X | N/A | |
0.13 | 3500. | X | N/A | |
0.14 | L | N/A | ||
0.16 | V | N/A | ||
0.23 | 5400. | M | N/A | |
0.16 | V | Bohon and Claussen, 1951 |
Gas phase ion energetics data
Go To: Top, Gas phase thermochemistry data, 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:
B - John E. Bartmess
MM - Michael M. Meot-Ner (Mautner)
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 C8H10+ (ion structure unspecified)
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
IE (evaluated) | 8.44 ± 0.05 | eV | N/A | N/A | L |
Quantity | Value | Units | Method | Reference | Comment |
Proton affinity (review) | 189.9 | kcal/mol | N/A | Hunter and Lias, 1998 | HL |
Quantity | Value | Units | Method | Reference | Comment |
Gas basicity | 183.3 | kcal/mol | N/A | Hunter and Lias, 1998 | HL |
Electron affinity determinations
EA (eV) | Reference | Comment |
---|---|---|
0.001519 ± 0.000087 | Hammer, Diri, et al., 2003 | B |
Proton affinity at 298K
Proton affinity (kcal/mol) | Reference | Comment |
---|---|---|
189.7 | Aue, Guidoni, et al., 2000 | Experimental literature data re-evaluated by the authors using ab initio protonation entropies; MM |
188.9 ± 0.26 | Fernandez, Jennings, et al., 1989 | T = 370 - 750K; Reference Sprot(CH3)2O = 16.5 J/mol K in Hunter and Lias, 1998 needs to be re-evaluated; MM |
Gas basicity at 298K
Gas basicity (review) (kcal/mol) | Reference | Comment |
---|---|---|
183.3 | Aue, Guidoni, et al., 2000 | Experimental literature data re-evaluated by the authors using ab initio protonation entropies; MM |
184.3 ± 0.33 | Fernandez, Jennings, et al., 1989 | T = 370 - 750K; Reference Sprot(CH3)2O = 16.5 J/mol K in Hunter and Lias, 1998 needs to be re-evaluated; MM |
Protonation entropy at 298K
Protonation entropy (cal/mol*K) | Reference | Comment |
---|---|---|
10.6 | Fernandez, Jennings, et al., 1989 | T = 370 - 750K; Reference Sprot(CH3)2O = 16.5 J/mol K in Hunter and Lias, 1998 needs to be re-evaluated; MM |
Ionization energy determinations
IE (eV) | Method | Reference | Comment |
---|---|---|---|
8.52 ± 0.01 | EQ | Lias and Ausloos, 1978 | LLK |
8.44 | PE | Bock, Kaim, et al., 1978 | LLK |
8.80 ± 0.05 | EI | Loudon and Mazengo, 1974 | LLK |
8.37 ± 0.02 | PE | Maier and Turner, 1973 | LLK |
8.52 | CTS | Kinoshita, 1962 | RDSH |
8.445 | PI | Bralsford, Harris, et al., 1960 | RDSH |
8.44 ± 0.02 | PI | Vilesov and Terenin, 1957 | RDSH |
8.445 ± 0.015 | PI | Watanabe, 1954 | RDSH |
8.48 | S | Hammond, Price, et al., 1950 | RDSH |
8.44 | PE | Howell, Goncalves, et al., 1984 | Vertical value; LBLHLM |
8.43 | PE | Koenig, Tuttle, et al., 1974 | Vertical value; LLK |
8.6 ± 0.03 | PE | Klessinger, 1972 | Vertical value; LLK |
Appearance energy determinations
Ion | AE (eV) | Other Products | Method | Reference | Comment |
---|---|---|---|---|---|
C5H5+ | 16.3 ± 0.2 | C2H2+CH3 | EI | Tajima and Tsuchiya, 1973 | LLK |
C7H7+ | 11.5 ± 0.3 | ? | EI | McLafferty and Winkler, 1974 | LLK |
C7H7+ | 11.9 ± 0.2 | CH3 | EI | Loudon and Mazengo, 1974 | LLK |
C7H7+ | 11.05 ± 0.05 | CH3 | PI | Akopyan and Vilesov, 1968 | RDSH |
C7H7+ | 11.3 ± 0.1 | CH3 | EI | Nounou, 1966 | RDSH |
C8H9+ | 12.1 ± 0.2 | H | EI | Loudon and Mazengo, 1974 | LLK |
C8H9+ | 11.35 ± 0.05 | H | PI | Akopyan and Vilesov, 1968 | RDSH |
C8H9+ | 11.9 ± 0.1 | H | EI | Tait, Shannon, et al., 1962 | RDSH |
De-protonation reactions
C8H9- + =
By formula: C8H9- + H+ = C8H10
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
ΔrH° | 381.9 ± 2.4 | kcal/mol | G+TS | Bartmess, Scott, et al., 1979 | gas phase; value altered from reference due to change in acidity scale; B |
Quantity | Value | Units | Method | Reference | Comment |
ΔrG° | 374.8 ± 2.3 | kcal/mol | IMRE | Bartmess, Scott, et al., 1979 | gas phase; value altered from reference due to change in acidity scale; B |
References
Go To: Top, Gas phase thermochemistry data, 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.
Prosen, Johnson, et al., 1946
Prosen, E.J.; Johnson, W.H.; Rossini, F.D.,
Heats of combustion and formation at 25°C of the alkylbenzenes through C10H14, and of the higher normal monoalkylbenzenes,
J. Res. NBS, 1946, 36, 455-461. [all data]
Chao J., 1986
Chao J.,
Thermodynamic properties of key organic oxygen compounds in the carbon range C1 to C4. Part 2. Ideal gas properties,
J. Phys. Chem. Ref. Data, 1986, 15, 1369-1436. [all data]
Pitzer K.S., 1943
Pitzer K.S.,
The thermodynamics and molecular structure of benzene and its methyl derivatives,
J. Am. Chem. Soc., 1943, 65, 803-829. [all data]
Taylor W.J., 1946
Taylor W.J.,
Heats, equilibrium constants, and free energies of formation of the alkylbenzenes,
J. Res. Nat. Bur. Stand., 1946, 37, 95-122. [all data]
Draeger J.A., 1981
Draeger J.A.,
Ideal gas thermodynamic properties of 1,4-dimethylbenzene,
J. Chem. Phys., 1981, 74, 4748-4749. [all data]
Draeger, 1985
Draeger, J.A.,
The methylbenzenes II. Fundamental vibrational shifts, statistical thermodynamic functions, and properties of formation,
J. Chem. Thermodyn., 1985, 17, 263-275. [all data]
Hossenlopp I.A., 1981
Hossenlopp I.A.,
Vapor heat capacities and enthalpies of vaporization of four aromatic and/or cycloalkane hydrocarbons,
J. Chem. Thermodyn., 1981, 13, 423-428. [all data]
Coops, Mulder, et al., 1946
Coops, J.; Mulder, D.; Dienske, J.W.; Smittenberg, J.,
The heats of combustion of a number of hydrocarbons,
Rec. Trav. Chim. Pays/Bas, 1946, 65, 128. [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]
Richards and Barry, 1915
Richards, T.W.; Barry, F.,
The heats of combustion of aromatic hydrocarbons and hexamethylene,
J. Am. Chem. Soc., 1915, 37, 993-1020. [all data]
Richards and Jesse, 1910
Richards, T.W.; Jesse, R.H., Jr.,
The heats of combustion of the octanes and xylenes,
J. Am. Chem. Soc., 1910, 32, 268-298. [all data]
Messerly, Finke, et al., 1988
Messerly, J.F.; Finke, H.L.; Good, W.D.; Gammon, B.E.,
Condensed-phase heat capacities and derived thermodynamic properties for 1,4-dimethylbenzene, 1,2-diphenylethane, and 2,3-dimethylnaphthalene,
J. Chem. Thermodynam., 1988, 20, 485-501. [all data]
Pitzer and Scott, 1943
Pitzer, K.S.; Scott, D.W.,
The thermodynamics and molecular structure of benzene and its methyl derivatives,
J. Am. Chem. Soc., 1943, 65, 803-829. [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]
Tardajos, Aicart, et al., 1986
Tardajos, G.; Aicart, E.; Costas, M.; Patterson, D.,
Liquid structure and second-order mixing functions for benzene, toluene, and p-xylene with n-alkanes, J. Chem. Soc.,
Faraday Trans., 1986, 1 82, 2977-2987. [all data]
Fortier and Benson, 1979
Fortier, J.-L.; Benson, G.C.,
Heat capacities of some binary aromatic hydrocarbon mixtures containing benzene or toluene,
J. Chem. Eng. Data, 1979, 24(1), 34-37. [all data]
Ott, Goates, et al., 1979
Ott, J.B.; Goates, J.R.; Grigg, R.B.,
Excess volumes, enthalpies, and Gibbs free energies for mixtures of benzenes + p-xylene,
J. Chem. Thermodynam., 1979, 11, 1167-1173. [all data]
Fortier and Benson, 1977
Fortier, J.-L.; Benson, G.C.,
Excess heat capacities of binary mixtures of tetrachloromethane witlh some aromatic liquids at 298.15 K,
J. Chem. Thermodynam., 1977, 9, 1181-1188. [all data]
Wilhelm, Grolier, et al., 1977
Wilhelm, E.; Grolier, J.-P.E.; Karbalai Ghassemi, M.H.,
Molar heat capacities of binary liquid mixtures: 1,2-dichloroethane + benzene, + toluene, and + p-xylene,
Ber. Bunsenges. Phys. Chem., 1977, 81, 925-930. [all data]
Hyder Khan and Subrahmanyam, 1971
Hyder Khan, V.; Subrahmanyam, S.V.,
Excess thermodynamic functions of the systems: benzene + p-xylene and benzene + p-dioxan,
Trans. Faraday Soc., 1971, 67, 2282-2291. [all data]
Swietoslawski and Zielenkiewicz, 1958
Swietoslawski, W.; Zielenkiewicz, A.,
Mean specific heats of binary positive azeotropes,
Bull. Acad. Pol. Sci. Ser. Sci. Chim., 1958, 6, 367-369. [all data]
Corruccini and Ginnings, 1947
Corruccini, R.J.; Ginnings, D.C.,
The enthalpy, entropy and specific heat of liquid p-xylene from 0 to 300°. The heat of fusion,
J. Am. Chem. Soc., 1947, 69, 2291-2294. [all data]
Kurbatov, 1947
Kurbatov, V.Ya.,
Specific heat of liquids. I. Specific heat of benzenoid hydrocarbons,
Zhur. Obshch. Khim., 1947, 17, 1999-2003. [all data]
Willams and Daniels, 1924
Willams, J.W.; Daniels, F.,
The specific heats of certain organic liquids at elevated temperatures,
J. Am. Chem. Soc., 1924, 46, 903-917. [all data]
Messerly, Finke, et al., 1988, 2
Messerly, J.F.; Finke, H.L.; Good, W.D.; Gammon, B.E.,
Condensed-phase heat capacities and derived thermodynamic properties for 1,4-dimethylbenzene, 1,2-diphenylethane, and 2,3-dimethylnaphthalene,
J. Chem. Thermodyn., 1988, 20, 485. [all data]
Huffman, Parks, et al., 1930, 2
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, 1547-58. [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]
Akhundov and Imanov, 1970
Akhundov, T.S.; Imanov, Sh.Yu.,
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Notes
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- Symbols used in this document:
AE Appearance energy Cp,gas Constant pressure heat capacity of gas Cp,liquid Constant pressure heat capacity of liquid EA Electron affinity IE (evaluated) Recommended ionization energy Pc Critical pressure S°liquid Entropy of liquid at standard conditions 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 ΔcH°liquid Enthalpy of combustion of liquid at standard conditions ΔfH°gas Enthalpy of formation of gas at standard conditions ΔfH°liquid Enthalpy of formation of liquid 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 ΔsubH Enthalpy 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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