- The Enthalpy Of Vaporization Of Benzene Is 33.9 At 298 Inches
- The Enthalpy Of Vaporization Of Benzene Is 33.9 At 298 Pounds
- The Enthalpy Of Vaporization Of Benzene Is 33.9 At 298 Feet
- The Enthalpy Of Vaporization Of Benzene Is 33.9 At 298 Divided
The normal boiling point of c2h5oh, is 78.3C and it's molar enthalpy of vaporization is 38.56 kj/mol. What is the change in enthropy in the system in J/K when 97.2 g of c2h5oh(g) at 1 atm condenses to liquid at the normal boiling point? The answer is -231. How do i get to that number? Please explain and thanks in advance!
A new group contribution method for estimating the enthalpy of vaporization at 298.15 K (ΔHV(298.15 K)) and at the normal boiling temperature (ΔHV(Tb)), as well as the entropy of vaporization at the normal boiling temperature (ΔSV(Tb)), of pure organic compounds has been developed. Large databases of critically assessed data have been used for group contribution calculations: data for 831. (a) Assuming benzene molecules contain three single and three double carbon − carbon bonds and use mean bond enthalpy data. (Mean bond enthalpies / kJ mol − 1: C − C, 347; C=C, 612; C − H, 412.) (b) The enthalpy change of combustion of liquid benzene at 298 K is − 3267.4 kJ mol − 1. The enthalpy change of vaporization of benzene is. The standard reaction enthalpy for the combustion of propane,. is −2220 kJ mol −1. Calculate the standard enthalpy of combustion of propene. Answer The combustion reaction we require is. This reaction can be recreated from the following sum:. Test 2.6 Calculate the enthalpy of hydrogenation of benzene from its enthalpy. Nine tells us that the normal boiling point of benzene is 80.1 to be selfishness on the heat of vaporization or adult H back is 30.7 killed. It asks us to calculate the boiling point of bendy and in Celsius on top of Mount Everest, where the pressure is equal to 260 millimeters mercury.
- Formula: C6H6
- Molecular weight: 78.1118
- IUPAC Standard InChI:
- InChI=1S/C6H6/c1-2-4-6-5-3-1/h1-6H
- Download the identifier in a file.
- IUPAC Standard InChIKey:UHOVQNZJYSORNB-UHFFFAOYSA-N
- CAS Registry Number: 71-43-2
- Chemical structure:
This structure is also available as a 2d Mol fileor as a computed3d SD file
The 3d structure may be viewed usingJavaorJavascript. - Isotopologues:
- Other names:[6]Annulene;Benzol;Benzole;Coal naphtha;Cyclohexatriene;Phenyl hydride;Pyrobenzol;Pyrobenzole;Benzolene;Bicarburet of hydrogen;Carbon oil;Mineral naphtha;Motor benzol;Benzeen;Benzen;Benzin;Benzine;Benzolo;Fenzen;NCI-C55276;Phene;Rcra waste number U019;UN 1114;NSC 67315;1,3,5-Cyclohexatriene
- Permanent link for this species. Use this link for bookmarking this speciesfor future reference.
- Information on this page:
- Other data available:
- Reaction thermochemistry data:reactions 1 to 50,reactions 51 to 99
- Data at other public NIST sites:
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Phase change data
Go To:Top, References, Notes
Data compilation copyrightby 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, Kenneth Kroenlein director
BS - Robert L. Brown and Stephen E. Stein
DRB - Donald R. Burgess, Jr.
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
AC - William E. Acree, Jr., James S. Chickos
DH - Eugene S. Domalski and Elizabeth D. Hearing
Quantity | Value | Units | Method | Reference | Comment |
---|---|---|---|---|---|
Tboil | 353.3 ± 0.1 | K | AVG | N/A | Average of 147 out of 183 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tfus | 278.64 ± 0.08 | K | AVG | N/A | Average of 57 out of 69 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Ttriple | 278.5 ± 0.6 | K | AVG | N/A | Average of 9 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Tc | 562.0 ± 0.8 | K | AVG | N/A | Average of 36 out of 41 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Pc | 48.9 ± 0.4 | bar | AVG | N/A | Average of 24 out of 26 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
Vc | 0.25 ± 0.03 | l/mol | AVG | N/A | Average of 6 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ρc | 3.9 ± 0.2 | mol/l | AVG | N/A | Average of 12 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ΔvapH° | 33.9 ± 0.1 | kJ/mol | AVG | N/A | Average of 10 out of 11 values; Individual data points |
Quantity | Value | Units | Method | Reference | Comment |
ΔsubH° | 44.4 | kJ/mol | TE,ME | Kruif, 1980 | Based on data from 183. - 197. K.; AC |
Enthalpy of vaporization
ΔvapH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
30.72 | 353.3 | N/A | Majer and Svoboda, 1985 | |
33.2 | 320. | N/A | Lubomska, Banas, et al., 2002 | Based on data from 305. - 345. K.; AC |
35.6 | 258. - 313. | GC | Liu and Dickhut, 1994 | AC |
33.5 | 311. | EB | Ambrose, Ewing, et al., 1990 | Based on data from 296. - 377. K.; AC |
33.4 | 307. | C | Dong, Lin, et al., 1988 | AC |
33.1 | 314. | C | Dong, Lin, et al., 1988 | AC |
32.4 | 324. | C | Dong, Lin, et al., 1988 | AC |
31.9 | 332. | C | Dong, Lin, et al., 1988 | AC |
31.4 | 344. | C | Dong, Lin, et al., 1988 | AC |
30.6 | 353. | C | Dong, Lin, et al., 1988 | AC |
34.4 | 294. | A | Stephenson and Malanowski, 1987 | Based on data from 279. - 377. K.; AC |
31.5 | 368. | A | Stephenson and Malanowski, 1987 | Based on data from 353. - 422. K.; AC |
30.2 | 435. | A | Stephenson and Malanowski, 1987 | Based on data from 420. - 502. K.; AC |
30.3 | 516. | A | Stephenson and Malanowski, 1987 | Based on data from 501. - 562. K.; AC |
30.8 | 352. | N/A | Natarajan, 1983 | AC |
30.5 | 361. | N/A | Natarajan, 1983 | AC |
30.2 | 366. | N/A | Natarajan, 1983 | AC |
35.3 | 343. | N/A | Tsonopoulos and Wilson, 1983 | Based on data from 313. - 373. K.; AC |
31. | 350. | N/A | Rao and Viswanath, 1977 | AC |
33.0 ± 0.1 | 313. | C | Svoboda, Veselý, et al., 1973 | AC |
32.2 ± 0.1 | 328. | C | Svoboda, Veselý, et al., 1973 | AC |
31.8 ± 0.1 | 333. | C | Svoboda, Veselý, et al., 1973 | AC |
31.4 ± 0.1 | 343. | C | Svoboda, Veselý, et al., 1973 | AC |
30.9 ± 0.1 | 353. | C | Svoboda, Veselý, et al., 1973 | AC |
32.6 ± 0.4 | 313. | DSC | Mita, Imai, et al., 1971 | AC |
32.5 ± 0.5 | 328. | DSC | Mita, Imai, et al., 1971 | AC |
31.6 ± 0.4 | 345. | DSC | Mita, Imai, et al., 1971 | AC |
34.1 | 299. | N/A | Forziati, Norris, et al., 1949 | Based on data from 284. - 354. K.; AC |
34.1 | 293. | N/A | Yarym-Agaev, Fedos'ev, et al., 1949 | AC |
34.1 | 297. | N/A | Thomson, 1946 | Based on data from 282. - 354. K.; AC |
31.2 | 294. | N/A | Scott and Brickwedde, 1945 | AC |
34.1 | 303. | MM | Willingham, Taylor, et al., 1945 | Based on data from 288. - 354. K.; AC |
33.4 | 313. | EB | Smith, 1941 | Based on data from 298. - 373. K.; AC |
34.5 | 288. | N/A | Stuckey and Saylor, 1940 | Based on data from 273. - 348. K.; AC |
Enthalpy of vaporization
ΔvapH = A exp(-αTr) (1 − Tr)β
ΔvapH = Enthalpy of vaporization (at saturation pressure) (kJ/mol)
Tr = reduced temperature (T / Tc)
View plotRequires a JavaScript / HTML 5 canvas capable browser.
Temperature (K) | 293. - 469. |
---|---|
A (kJ/mol) | 47.41 |
α | 0.1231 |
β | 0.3602 |
Tc (K) | 562.1 |
Reference | Majer and Svoboda, 1985 |
Antoine Equation Parameters
log10(P) = A − (B / (T + C))
P = vapor pressure (bar)
T = temperature (K)
View plotRequires a JavaScript / HTML 5 canvas capable browser.
Temperature (K) | A | B | C | Reference | Comment |
---|---|---|---|---|---|
333.4 - 373.5 | 4.72583 | 1660.652 | -1.461 | Eon, Pommier, et al., 1971 | Coefficents calculated by NIST from author's data. |
297.9 - 318. | 0.14591 | 39.165 | -261.236 | Deshpande and Pandya, 1967 | Coefficents calculated by NIST from author's data. |
421.56 - 554.8 | 4.60362 | 1701.073 | 20.806 | Kalafati, Rasskazov, et al., 1967 | Coefficents calculated by NIST from author's data. |
287.70 - 354.07 | 4.01814 | 1203.835 | -53.226 | Williamham, Taylor, et al., 1945 |
Enthalpy of sublimation
ΔsubH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
41.7 | 258. - 273. | N/A | Liu and Dickhut, 1994 | AC |
45.2 | 264. | A | Stephenson and Malanowski, 1987 | Based on data from 223. - 279. K. See also Ha, Morrison, et al., 1976.; AC |
45.1 | 278. | N/A | Hessler, 1984 | AC |
53.9 ± 0.8 | 193. | N/A | De Kruif and Van Ginkel, 1977 | AC |
49.4 ± 0.4 | 193. | N/A | De Kruif and Van Ginkel, 1977 | AC |
45.6 | 279. | MM | Jackowski, 1974 | Based on data from 221. - 268. K.; AC |
44.1 | 261. | N/A | Jones, 1960 | AC |
43.1 | 229. | N/A | Jones, 1960 | AC |
44.6 | 279. | N/A | Milazzo, 1956 | AC |
46.6 | 282. | A | Stull, 1947 | Based on data from 263. - 270. K.; AC |
38. | 303. | V | Wolf and Weghofer, 1938 | ALS |
44.6 | 273. | N/A | de Boer, 1936 | See also Jackowski, 1974.; AC |
43.3 | 226. | A | Mündel, 1913 | Based on data from 214. - 238. K.; AC |
Enthalpy of fusion
ΔfusH (kJ/mol) | Temperature (K) | Method | Reference | Comment |
---|---|---|---|---|
9.8663 | 278.69 | N/A | Oliver, Eaton, et al., 1948 | DH |
9.916 | 278.65 | N/A | Ziegler and Andrews, 1942 | DH |
9.87 | 278.7 | C | Domalski and Hearing, 1996 | See also Andrews, Lynn, et al., 1926 and Ziegler and Andrews, 1942.; AC |
9.300 | 279.1 | N/A | Smith, 1979 | DH |
8.950 | 278.8 | N/A | Pacor, 1967 | DH |
9.937 | 278.6 | N/A | Tschamler, 1948 | DH |
9.803 | 278.6 | N/A | Huffman, Parks, et al., 1930 | DH |
9.875 | 278.55 | N/A | Andrews, Lynn, et al., 1926 | DH |
10.000 | 278.64 | N/A | Maass and Walbauer, 1925 | DH |
Entropy of fusion
ΔfusS (J/mol*K) | Temperature (K) | Reference | Comment |
---|---|---|---|
35.40 | 278.69 | Oliver, Eaton, et al., 1948 | DH |
35.59 | 278.65 | Ziegler and Andrews, 1942 | DH |
33.3 | 279.1 | Smith, 1979 | DH |
32.1 | 278.8 | Pacor, 1967 | DH |
35.19 | 278.6 | Huffman, Parks, et al., 1930 | DH |
35.5 | 278.55 | Andrews, Lynn, et al., 1926 | DH |
35.9 | 278.64 | Maass and Walbauer, 1925 | DH |
In addition to the Thermodynamics Research Center(TRC) data available from this site, much more physicaland chemical property data is available from thefollowing TRC products:
References
Go To:Top, Phase change data, Notes
Data compilation copyrightby the U.S. Secretary of Commerce on behalf of the U.S.A.All rights reserved.
Kruif, 1980
Kruif, C.G.,Enthalpies of sublimation and vapour pressures of 11 polycyclic hydrocarbons,J. Chem. Thermodyn., 1980, 12, 243-248. [all data]
Majer and Svoboda, 1985
Majer, V.; Svoboda, V.,Enthalpies of Vaporization of Organic Compounds: A Critical Review and Data Compilation, Blackwell Scientific Publications, Oxford, 1985, 300. [all data]
Lubomska, Banas, et al., 2002
Lubomska, Monika; Banas, Agnieszka; Malanowski, Stanislaw K.,Vapor-Liquid Equilibrium in Binary Systems Formed by Allyl Alcohol with Benzene and with Cyclohexane,J. Chem. Eng. Data, 2002, 47, 6, 1466-1471, https://doi.org/10.1021/je025540l. [all data]
The Enthalpy Of Vaporization Of Benzene Is 33.9 At 298 Inches
Liu and Dickhut, 1994
Liu, Kewen; Dickhut, Rebecca M.,Saturation vapor pressures and thermodynamic properties of benzene and selected chlorinated benzenes at environmental temperatures,Chemosphere, 1994, 29, 3, 581-589, https://doi.org/10.1016/0045-6535(94)90445-6. [all data]
Ambrose, Ewing, et al., 1990
Ambrose, D.; Ewing, M.B.; Ghiassee, N.B.; Sanchez Ochoa, J.C.,The ebulliometric method of vapour-pressure measurement: vapour pressures of benzene, hexafluorobenzene, and naphthalene,The Journal of Chemical Thermodynamics, 1990, 22, 6, 589-605, https://doi.org/10.1016/0021-9614(90)90151-F. [all data]
Dong, Lin, et al., 1988
Dong, Jin-Quan; Lin, Rui-Sen; Yen, Wen-Hsing,Heats of vaporization and gaseous molar heat capacities of ethanol and the binary mixture of ethanol and benzene,Can. J. Chem., 1988, 66, 4, 783-790, https://doi.org/10.1139/v88-136. [all data]
Stephenson and Malanowski, 1987
Stephenson, Richard M.; Malanowski, Stanislaw,Handbook of the Thermodynamics of Organic Compounds, 1987, https://doi.org/10.1007/978-94-009-3173-2. [all data]
Natarajan, 1983
Natarajan, G.,High-temperature calorimeter for the measurement of vapor pressure and enthalpy of vaporization,Rev. Sci. Instrum., 1983, 54, 9, 1175, https://doi.org/10.1063/1.1137545. [all data]
Tsonopoulos and Wilson, 1983
Tsonopoulos, Constantine; Wilson, G.M.,High-temperature mutual solubilities of hydrocarbons and water. Part I: Benzene, cyclohexane andn-hexane,AIChE J., 1983, 29, 6, 990-999, https://doi.org/10.1002/aic.690290618. [all data]
Rao and Viswanath, 1977
Rao, Yaddanapudi J.; Viswanath, Dabir S.,Integral isobaric heats of vaporization of benzene-chloroethane systems,J. Chem. Eng. Data, 1977, 22, 1, 36-38, https://doi.org/10.1021/je60072a011. [all data]
Svoboda, Veselý, et al., 1973
Svoboda, V.; Veselý, F.; Holub, R.; Pick, J.,Enthalpy data of liquids. II. The dependence of heats of vaporization of methanol, propanol, butanol, cyclohexane, cyclohexene, and benzene on temperature,Collect. Czech. Chem. Commun., 1973, 38, 12, 3539-3543, https://doi.org/10.1135/cccc19733539. [all data]
Mita, Imai, et al., 1971
Mita, Itaru; Imai, Isao; Kambe, Hirotaro,Determination of heat of mixing and heat of vaporization with a differential scanning calorimeter,Thermochimica Acta, 1971, 2, 4, 337-344, https://doi.org/10.1016/0040-6031(71)85035-9. [all data]
Forziati, Norris, et al., 1949
Forziati, Alphonse F.; Norris, William R.; Rossini, Frederick D.,Vapor pressures and boiling points of sixty API-NBS hydrocarbons,J. RES. NATL. BUR. STAN., 1949, 43, 6, 555-17, https://doi.org/10.6028/jres.043.050. [all data]
Yarym-Agaev, Fedos'ev, et al., 1949
Yarym-Agaev, N.L.; Fedos'ev, N.N.; Skorikov, K.G.,Zh. Fiz. Khim., 1949, 11, 1257. [all data]
Thomson, 1946
Thomson, George Wm.,The Antoine Equation for Vapor-pressure Data.,Chem. Rev., 1946, 38, 1, 1-39, https://doi.org/10.1021/cr60119a001. [all data]
Scott and Brickwedde, 1945
Scott, R.B.; Brickwedde, F.G.,Thermodynamic properties of solid and liquid ethylbenzene from 0 to 300 degrees K,J. RES. NATL. BUR. STAN., 1945, 35, 6, 501-17, https://doi.org/10.6028/jres.035.024. [all data]
Willingham, Taylor, et al., 1945
Willingham, C.B.; Taylor, W.J.; Pignocco, J.M.; Rossini, F.D.,Vapor pressures and boiling points of some paraffin, alkylcyclopentane, alkylcyclohexane, and alkylbenzene hydrocarbons,J. RES. NATL. BUR. STAN., 1945, 35, 3, 219-17, https://doi.org/10.6028/jres.035.009. [all data]
Smith, 1941
Smith, E.R.,Boiling points of benzene, 2,2,3-trimethylbutane, 3-ethylpentane, and 2,2,4,4-tetramethylpentane within the range 100 to 1,500 millimeters of mercury,J. RES. NATL. BUR. STAN., 1941, 26, 2, 129-17, https://doi.org/10.6028/jres.026.004. [all data]
Stuckey and Saylor, 1940
Stuckey, James M.; Saylor, John H.,The Vapor Pressures of Some Organic Compounds. I. 1,J. Am. Chem. Soc., 1940, 62, 11, 2922-2925, https://doi.org/10.1021/ja01868a011. [all data]
Eon, Pommier, et al., 1971
Eon, C.; Pommier, C.; Guiochon, G.,Vapor pressures and second virial coefficients of some five-membered heterocyclic derivatives,J. Chem. Eng. Data, 1971, 16, 4, 408-410, https://doi.org/10.1021/je60051a008. [all data]
Deshpande and Pandya, 1967
Deshpande, D.D.; Pandya, M.V.,Thermodynamics of Binary Solutions. Part 2. Vapour Pressures and Excess Free Energies of Aniline Solutions,Trans. Faraday Soc., 1967, 63, 2149-2157, https://doi.org/10.1039/tf9676302149. [all data]
Kalafati, Rasskazov, et al., 1967
Kalafati, D.D.; Rasskazov, D.S.; Petrov, E.K.,Experimental Determination of a Dependence of a Saturated Vapor Pressure of Benzene on Temperature,Zh. Fiz. Khim., 1967, 41, 1357-1359. [all data]
Williamham, Taylor, et al., 1945
Williamham, C.B.; Taylor, W.J.; Pignocco, J.M.; Rossini, F.D.,Vapor Pressures and Boiling Points of Some Paraffin, Alkylcyclopentane, Alkylcyclohexane, and Alkylbenzene Hydrocarbons,J. Res. Natl. Bur. Stand. (U.S.), 1945, 35, 3, 219-244, https://doi.org/10.6028/jres.035.009. [all data]
Ha, Morrison, et al., 1976
Ha, H.; Morrison, J.A.; Richards, E.L.,Vapour pressures of solid benzene, cyclohexane and their mixtures,J. Chem. Soc., Faraday Trans. 1, 1976, 72, 0, 1051, https://doi.org/10.1039/f19767201051. [all data]
Hessler, 1984
Hessler, W.,Wiss. Zeitschr. Wilhelm-Pieck-Univ. Rostock, Naturwiss. Reihe, 1984, 33, 9. [all data]
De Kruif and Van Ginkel, 1977
De Kruif, C.G.; Van Ginkel, C.H.D.,Torsion-weighing effusion vapour-pressure measurements on organic compounds,The Journal of Chemical Thermodynamics, 1977, 9, 8, 725-730, https://doi.org/10.1016/0021-9614(77)90015-5. [all data]
Jackowski, 1974
Jackowski, A.W.,Vapour pressures of solid benzene and of solid cyclohexane,The Journal of Chemical Thermodynamics, 1974, 6, 1, 49-52, https://doi.org/10.1016/0021-9614(74)90205-5. [all data]
Jones, 1960
Jones, A.H.,Sublimation Pressure Data for Organic Compounds.,J. Chem. Eng. Data, 1960, 5, 2, 196-200, https://doi.org/10.1021/je60006a019. [all data]
Milazzo, 1956
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Stull, 1947
Stull, Daniel R.,Vapor Pressure of Pure Substances. Organic and Inorganic Compounds,Ind. Eng. Chem., 1947, 39, 4, 517-540, https://doi.org/10.1021/ie50448a022. [all data]
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Wolf, K.L.; Weghofer, H.,Uber sublimationswarmen,Z. Phys. Chem., 1938, 39, 194-208. [all data]
de Boer, 1936
de Boer, J.H.,The influence of van der Waals' forces and primary bonds on binding energy, strength and orientation, with special reference to some artificial resins,Trans. Faraday Soc., 1936, 32, 10, https://doi.org/10.1039/tf9363200010. [all data]
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Mündel, C.F.,Z. Phys. Chem., Stoechiom. Verwandtschaftsl., 1913, 85, 435. [all data]
Oliver, Eaton, et al., 1948
Oliver, G.D.; Eaton, M.; Huffman, H.M.,The heat capacity, heat of fusion and entropy of benzene,J. Am. Chem. Soc., 1948, 70, 1502-1505. [all data]
Ziegler and Andrews, 1942
Ziegler, W.T.; Andrews, D.H.,The heat capacity of benzene-d6,J. Am. Chem. Soc., 1942, 64, 2482-2485. [all data]
Domalski and Hearing, 1996
Domalski, Eugene S.; Hearing, Elizabeth D.,Heat Capacities and Entropies of Organic Compounds in the Condensed Phase. Volume III,J. Phys. Chem. Ref. Data, 1996, 25, 1, 1, https://doi.org/10.1063/1.555985. [all data]
Andrews, Lynn, et al., 1926
Andrews, D.H.; Lynn, G.; Johnston, J.,The heat capacities and heat of crystallization of some isomeric aromatic compounds,J. Am. Chem. Soc., 1926, 48, 1274-1287. [all data]
Smith, 1979
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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]
Tschamler, 1948
Tschamler, H.,Uber binare flussige Mischungen I. Mischungswarment, Volumseffekte und Zustandsdiagramme von chlorex mit benzol und n-alkylbenzolen,Monatsh. Chem., 1948, 79, 162-177. [all data]
Huffman, Parks, et al., 1930
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The Enthalpy Of Vaporization Of Benzene Is 33.9 At 298 Pounds
Notes
The Enthalpy Of Vaporization Of Benzene Is 33.9 At 298 Feet
Go To:Top, Phase change data, References
The Enthalpy Of Vaporization Of Benzene Is 33.9 At 298 Divided
- Symbols used in this document:
Pc Critical pressure Tboil Boiling point Tc Critical temperature Tfus Fusion (melting) point Ttriple Triple point temperature Vc Critical volume ΔfusH Enthalpy of fusion ΔfusS Entropy of fusion ΔsubH Enthalpy of sublimation ΔsubH° Enthalpy of sublimation at standard conditions 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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