Ethanol

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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 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-234. ± 2.kJ/molAVGN/AAverage of 9 values; Individual data points
Quantity Value Units Method Reference Comment
ΔcH°gas-1366.3 ± 0.4kJ/molCmRossini, 1932Flame Calorimetry; Corresponding ΔfHºgas = -278.20 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS

Constant pressure heat capacity of gas

Cp,gas (J/mol*K) Temperature (K) Reference Comment
37.1250.Thermodynamics Research Center, 1997p=1 bar. Recommended entropies and heat capacities are in close agreement with other statistically calculated values [ Zhuravlev E.Z., 1959, Chermin H.A.G., 1961, Green J.H.S., 1961, Green J.H.S., 1961, 2, Chao J., 1986, Gurvich, Veyts, et al., 1989]. Please also see Chao J., 1986, 2.; GT
41.70100.
46.94150.
52.02200.
61.46273.15
65.21 ± 0.14298.15
65.49300.
81.22400.
95.78500.
108.24600.
118.83700.
127.92800.
135.81900.
142.681000.
148.681100.
153.921200.
158.491300.
162.501400.
166.011500.
173.01750.
178.22000.
182.02250.
184.92500.
187.2750.
189.3000.

Constant pressure heat capacity of gas

Cp,gas (J/mol*K) Temperature (K) Reference Comment
51.38 ± 0.50200.Stromsoe E., 1970Experimental data [ Bennewitz K., 1938, Eucken A., 1948, Barrow G.M., 1952, Sinke G.C., 1953, Halford J.O., 1957] are collected in ref. [ Green J.H.S., 1961]. Ideal gas heat capacities are given by [ Stromsoe E., 1970] as a linear function Cp=f1*(a+bT). This expression approximates the experimental values with the average deviation of 1.09 J/mol*K. The accuracy of the experimental heat capacities [ Stromsoe E., 1970] is estimated as less than 0.3%. Please also see Green J.H.S., 1961, Counsell J.F., 1970.; GT
62.30 ± 0.54279.
62.09 ± 0.42280.
73.15350.01
75.7 ± 1.1356.55
74.57360.00
76.4 ± 1.1361.75
75.52367.9
76.00370.01
77.7 ± 1.1371.85
77.46380.00
79.8 ± 1.1387.25
80.0 ± 1.1388.85
80.40400.08
82.01410.16
83.39422.
84.10425.09
85.9 ± 1.1433.25
87.99437.
87.3 ± 1.1443.35
87.65450.08
91.11475.12
91.21476.
92.2 ± 1.1480.45
99.4 ± 1.1534.35
101.3 ± 1.1548.75
104.5 ± 1.1572.25
107.0 ± 1.1591.25

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
DH - Eugene S. Domalski and Elizabeth D. Hearing
AC - William E. Acree, Jr., James S. Chickos
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
DRB - Donald R. Burgess, Jr.
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
Tboil351.5 ± 0.2KAVGN/AAverage of 138 out of 148 values; Individual data points
Quantity Value Units Method Reference Comment
Tfus159. ± 2.KAVGN/AAverage of 11 values; Individual data points
Quantity Value Units Method Reference Comment
Ttriple150. ± 20.KAVGN/AAverage of 8 values; Individual data points
Quantity Value Units Method Reference Comment
Tc514. ± 7.KAVGN/AAverage of 37 out of 38 values; Individual data points
Quantity Value Units Method Reference Comment
Pc63. ± 4.barAVGN/AAverage of 18 out of 19 values; Individual data points
Quantity Value Units Method Reference Comment
Vc0.168l/molN/AGude and Teja, 1995 
Quantity Value Units Method Reference Comment
ρc6.0 ± 0.2mol/lAVGN/AAverage of 7 values; Individual data points
Quantity Value Units Method Reference Comment
ΔvapH°42.3 ± 0.4kJ/molAVGN/AAverage of 12 out of 13 values; Individual data points

Enthalpy of vaporization

ΔvapH (kJ/mol) Temperature (K) Method Reference Comment
38.56351.5N/AMajer and Svoboda, 1985 
41.7326.N/AMejia, Segura, et al., 2010Based on data from 311. to 351. K.; AC
39.3338.N/AAucejo, Loras, et al., 1999Based on data from 323. to 357. K.; AC
40.7321.EBDiogo, Santos, et al., 1995Based on data from 309. to 343. K.; AC
40.5357.N/AOrtega, Susial, et al., 1990Based on data from 342. to 357. K.; AC
35.2393.CVine and Wormald, 1989AC
30.6423.CVine and Wormald, 1989AC
25.7453.CVine and Wormald, 1989AC
21.8473.CVine and Wormald, 1989AC
17.3493.CVine and Wormald, 1989AC
14.2503.CVine and Wormald, 1989AC
40.9320.CDong, Lin, et al., 1988AC
40.4328.CDong, Lin, et al., 1988AC
40.2335.CDong, Lin, et al., 1988AC
39.4344.CDong, Lin, et al., 1988AC
38.8351.CDong, Lin, et al., 1988AC
41.3335.AStephenson and Malanowski, 1987Based on data from 320. to 359. K.; AC
45.6256.AStephenson and Malanowski, 1987Based on data from 210. to 271. K.; AC
44.208.AStephenson and Malanowski, 1987Based on data from 193. to 223. K.; AC
41.3335.AStephenson and Malanowski, 1987Based on data from 320. to 359. K.; AC
40.1361.AStephenson and Malanowski, 1987Based on data from 349. to 374. K.; AC
39.1385.AStephenson and Malanowski, 1987Based on data from 370. to 464. K.; AC
36.1474.AStephenson and Malanowski, 1987Based on data from 459. to 514. K.; AC
42.5307.AStephenson and Malanowski, 1987Based on data from 292. to 353. K.; AC
42.5308.A,EBStephenson and Malanowski, 1987Based on data from 293. to 366. K. See also Ambrose, Counsell, et al., 1970.; AC
42.9286.N/AWilhoit and Zwolinski, 1973Based on data from 271. to 373. K.; AC
41.0 ± 0.1320.CCounsell, Fenwick, et al., 1970AC
40.0 ± 0.1335.CCounsell, Fenwick, et al., 1970AC
38.7 ± 0.1351.CCounsell, Fenwick, et al., 1970AC
42.4303.N/AVan Ness, Soczek, et al., 1967Based on data from 288. to 348. K.; AC
42.2313.N/AKretschmer and Wiebe, 1949Based on data from 298. to 351. K.; AC
40.0351.N/AOguri, Anjo, et al., 1934AC
54.1301.N/AKahlbaum, 1883Based on data from 286. to 351. 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)

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Temperature (K) 298. to 469.
A (kJ/mol) 50.43
α -0.4475
β 0.4989
Tc (K) 513.9
ReferenceMajer and Svoboda, 1985

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
364.8 to 513.914.925311432.526-61.819Ambrose, Sprake, et al., 1975Coefficents calculated by NIST from author's data.
292.77 to 366.635.246771598.673-46.424Ambrose and Sprake, 1970Coefficents calculated by NIST from author's data.
273. to 351.705.372291670.409-40.191Kretschmer and Wiebe, 1949Coefficents calculated by NIST from author's data.

Enthalpy of fusion

ΔfusH (kJ/mol) Temperature (K) Reference Comment
4.973159.Yoshida, 1944DH
5.021158.5Kelley, 1929DH
4.626156.2Gibson, Parks, et al., 1920DH
4.64158.8Domalski and Hearing, 1996AC
4.962158.7Parks, 1925DH

Entropy of fusion

ΔfusS (J/mol*K) Temperature (K) Reference Comment
31.3159.Yoshida, 1944DH
31.68158.5Kelley, 1929DH
21.22158.7Parks, 1925DH

Entropy of fusion

ΔfusS (J/mol*K) Temperature (K) Reference Comment
28.16111.4Domalski and Hearing, 1996CAL
29.25158.8
5.2127.5
31.0159.

Enthalpy of phase transition

ΔHtrs (kJ/mol) Temperature (K) Initial Phase Final Phase Reference Comment
0.659127.5crystaline, IIliquidHaida, Suga, et al., 1977DH
4.931159.00crystaline, IliquidHaida, Suga, et al., 1977DH
3.138111.4crystaline, IIcrystaline, INikolaev, Rabinovich, et al., 1967DH
4.644158.8crystaline, IliquidNikolaev, Rabinovich, et al., 1967DH

Entropy of phase transition

ΔStrs (J/mol*K) Temperature (K) Initial Phase Final Phase Reference Comment
5.19127.5crystaline, IIliquidHaida, Suga, et al., 1977DH
31.01159.00crystaline, IliquidHaida, Suga, et al., 1977DH
28.17111.4crystaline, IIcrystaline, INikolaev, Rabinovich, et al., 1967DH
29.24158.8crystaline, IliquidNikolaev, Rabinovich, et al., 1967DH

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:

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
120. QN/A missing citation give several references for the Henry's law constants but don't assign them to specific species.
200. XN/A 
190.6600.MN/A 
200. XN/AValue given here as quoted by missing citation.
230. MN/A 
150.6400.XN/A 
220. MN/A 
160. M,XTimmermans, 1960Value given here as quoted by missing citation.
190. MButler, Ramchandani, et al., 1935 

Gas phase ion energetics data

Go To: Top, Gas 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)
LL - Sharon G. Lias and Joel F. Liebman
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 C2H6O+ (ion structure unspecified)

Quantity Value Units Method Reference Comment
IE (evaluated)10.48 ± 0.07eVN/AN/AL
Quantity Value Units Method Reference Comment
Proton affinity (review)776.4kJ/molN/AHunter and Lias, 1998HL
Quantity Value Units Method Reference Comment
Gas basicity746.kJ/molN/AHunter and Lias, 1998HL

Proton affinity at 298K

Proton affinity (kJ/mol) Reference Comment
779.4 ± 0.8Tabrizchi and Shooshtari, 2003T = 403-453K; Authors report only relative PAs. Absolute values are referenced here to PA(CH3COOC2H5) = 835.7 kJ/mol as listed in Hunter and Lias, 1998, although average PA(CH3COOC2H5) from the literature sources in Hunter and Lias, 1998 is 831.0 kJ/mol; MM

Ionization energy determinations

IE (eV) Method Reference Comment
10.41 ± 0.05EIHolmes and Lossing, 1991LL
10.4PEOhno, Imai, et al., 1985LBLHLM
10.47 ± 0.07EIBowen and Maccoll, 1984LBLHLM
10.3PEOhno, Imai, et al., 1983LBLHLM
10.5EIMishchanchuk, Pokrovskii, et al., 1982LBLHLM
10.7PEVon Niessen, Bieri, et al., 1980LLK
10.49 ± 0.01PIPotapov and Sorokin, 1972LLK
10.46 ± 0.02PECocksey, Eland, et al., 1971LLK
10.65PEBaker, Betteridge, et al., 1971LLK
10.46PEDewar and Worley, 1969RDSH
10.47 ± 0.02PIRefaey and Chupka, 1968RDSH
10.48 ± 0.05PIWatanabe, Nakayama, et al., 1962RDSH
10.64PEOhno, Imai, et al., 1985Vertical value; LBLHLM
10.64PEUtsunomiya, Kobayashi, et al., 1980Vertical value; LLK
10.65PEHoppilliard and Solgadi, 1980Vertical value; LLK
10.61PEBenoit and Harrison, 1977Vertical value; LLK
10.65 ± 0.03PEPeel and Willett, 1975Vertical value; LLK
10.59PEVovna, Lopatin, et al., 1974Vertical value; LLK
10.04PESchweig and Thiel, 1974Vertical value; LLK
10.62PERobin and Kuebler, 1973Vertical value; LLK
10.64PEKatsumata, Iwai, et al., 1973Vertical value; LLK

Appearance energy determinations

Ion AE (eV) Other Products MethodReferenceComment
C+22.9 ± 0.5H2+H+CH2OHEIStepanov, Perov, et al., 1988LL
CH2O+11.70CH4PIRefaey and Chupka, 1968RDSH
CH3+14.70 ± 0.10?EIHaney and Franklin, 1969RDSH
CH3O+11.25 ± 0.09CH3EIBowen and Maccoll, 1984LBLHLM
CH3O+11.40 ± 0.06CH3EISelim and Helal, 1981LLK
CH3O+11.30CH3EILossing, 1977LLK
CH3O+11.20 ± 0.05CH3PIPotapov and Sorokin, 1972LLK
CH3O+11.25CH3PIRefaey and Chupka, 1968RDSH
C2H3+14.7?EIFriedman, Long, et al., 1957RDSH
C2H3O+14.5H2+HEIFriedman, Long, et al., 1957RDSH
C2H4+12.0 ± 0.9H2OEIBowen and Maccoll, 1984LBLHLM
C2H4+12.0H2OPIRefaey and Chupka, 1968RDSH
C2H4O+~10.45H2EIHolmes, Terlouw, et al., 1976LLK
C2H5+12.7OHPIRefaey and Chupka, 1968RDSH
C2H5O+10.78 ± 0.09HEIBowen and Maccoll, 1984LBLHLM
C2H5O+10.6HEIMishchanchuk, Pokrovskii, et al., 1982LBLHLM
C2H5O+10.67HEILossing, 1977LLK
C2H5O+10.75 ± 0.03HEISolka and Russell, 1974LLK
C2H5O+10.80 ± 0.05HPIPotapov and Sorokin, 1972LLK
C2H5O+10.78 ± 0.02HPIRefaey and Chupka, 1968RDSH
C2H5O+[CH3CHOH+]10.801 ± 0.005HPIRuscic and Berkowitz, 1994T = 0K; LL
H+21.0 ± 0.5CH2+CH2OHEIStepanov, Perov, et al., 1988LL
H2O+13.06C2H4EILewis and Hamill, 1970RDSH
H3O+13.8H2+C2H3PIPECONiwa, Nishimura, et al., 1982LBLHLM
H3O+14.30 ± 0.02?EIHaney and Franklin, 1969, 2RDSH
O+21.7 ± 0.52CH3EIStepanov, Perov, et al., 1988LL

De-protonation reactions

C2H5O- + Hydrogen cation = Ethanol

By formula: C2H5O- + H+ = C2H6O

Quantity Value Units Method Reference Comment
ΔrH°1587. ± 4.2kJ/molD-EARamond, Davico, et al., 2000gas phase; B
ΔrH°1582. ± 8.4kJ/molCIDCHaas and Harrison, 1993gas phase; Both metastable and 50 eV collision energy.; B
ΔrH°1579. ± 8.8kJ/molG+TSBartmess, Scott, et al., 1979gas phase; value altered from reference due to change in acidity scale; B
ΔrH°1586.2 ± 0.42kJ/molCIDTDeTuri and Ervin, 1999gas phase; B
Quantity Value Units Method Reference Comment
ΔrG°1559. ± 4.6kJ/molH-TSRamond, Davico, et al., 2000gas phase; B
ΔrG°1554. ± 8.8kJ/molH-TSHaas and Harrison, 1993gas phase; Both metastable and 50 eV collision energy.; B
ΔrG°1551. ± 8.4kJ/molIMREBartmess, Scott, et al., 1979gas phase; value altered from reference due to change in acidity scale; B

Anion protonation reactions

C2H5O- + Hydrogen cation = Ethanol

By formula: C2H5O- + H+ = C2H6O

Quantity Value Units Method Reference Comment
ΔrH°1587. ± 4.2kJ/molD-EARamond, Davico, et al., 2000gas phase; B
ΔrH°1582. ± 8.4kJ/molCIDCHaas and Harrison, 1993gas phase; Both metastable and 50 eV collision energy.; B
ΔrH°1579. ± 8.8kJ/molG+TSBartmess, Scott, et al., 1979gas phase; value altered from reference due to change in acidity scale; B
ΔrH°1586.2 ± 0.42kJ/molCIDTDeTuri and Ervin, 1999gas phase; B
Quantity Value Units Method Reference Comment
ΔrG°1559. ± 4.6kJ/molH-TSRamond, Davico, et al., 2000gas phase; B
ΔrG°1554. ± 8.8kJ/molH-TSHaas and Harrison, 1993gas phase; Both metastable and 50 eV collision energy.; B
ΔrG°1551. ± 8.4kJ/molIMREBartmess, Scott, et al., 1979gas phase; value altered from reference due to change in acidity scale; B

References

Go To: Top, Gas 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.

Rossini, 1932
Rossini, F.D., The heats of combustion of methyl and ethyl alcohols, J. Res. NBS, 1932, 8, 119-139. [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]

Zhuravlev E.Z., 1959
Zhuravlev E.Z., Isotopic effect on thermodynamic functions of some organic deuterocompounds in the ideal gas state, Tr. Khim. i Khim. Tekhnol., 1959, 2, 475-485. [all data]

Chermin H.A.G., 1961
Chermin H.A.G., Thermo data for petrochemicals. Part 28. Gaseous normal alcohols. The important thermo properties are presented for all the gaseous normal alcohols from methanol through n-decanol, Petrol. Refiner, 1961, 40 (4), 127-130. [all data]

Green J.H.S., 1961
Green J.H.S., Thermodynamic properties of organic oxygen compounds. Part 5. Ethyl alcohol, Trans. Faraday Soc., 1961, 57, 2132-2137. [all data]

Green J.H.S., 1961, 2
Green J.H.S., Thermodynamic properties of the normal alcohols C1-C12, J. Appl. Chem., 1961, 11, 397-404. [all data]

Chao J., 1986
Chao J., Ideal gas thermodynamic properties of simple alkanols, Int. J. Thermophys., 1986, 7, 431-442. [all data]

Gurvich, Veyts, et al., 1989
Gurvich, L.V.; Veyts, I.V.; Alcock, C.B., Thermodynamic Properties of Individual Substances, 4th ed.; Vols. 1 and 2, Hemisphere, New York, 1989. [all data]

Chao J., 1986, 2
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]

Stromsoe E., 1970
Stromsoe E., Heat capacity of alcohol vapors at atmospheric pressure, J. Chem. Eng. Data, 1970, 15, 286-290. [all data]

Bennewitz K., 1938
Bennewitz K., Molar heats of vapor organic compounds, Z. Phys. Chem. (Leipzig), 1938, B39, 126-144. [all data]

Eucken A., 1948
Eucken A., Rotational hindrance in ether and alcohol molecules on the basis of heat capacity determinations, Z. Elektrochem., 1948, 52, 195-204. [all data]

Barrow G.M., 1952
Barrow G.M., Heat capacity, gas imperfection, infrared spectra, and internal rotation barriers of ethyl alcohol, J. Chem. Phys., 1952, 20, 1739-1744. [all data]

Sinke G.C., 1953
Sinke G.C., The heat capacity of organic vapors. VIII. Data for some aliphatic alcohols using an improved flow calorimeter requiring only 25 ml of sample, J. Am. Chem. Soc., 1953, 75, 1815-1818. [all data]

Halford J.O., 1957
Halford J.O., Standard heat capacities of gaseous methanol, ethanol, methane and ethane at 279 K by thermal conductivity, J. Phys. Chem., 1957, 61, 1536-1539. [all data]

Counsell J.F., 1970
Counsell J.F., Thermodynamic properties of organic oxygen compounds. 24. Vapor heat capacities and enthalpies of vaporization of ethanol, 2-methyl-1-propanol, and 1-pentanol, J. Chem. Thermodyn., 1970, 2, 367-372. [all data]

Gude and Teja, 1995
Gude, M.; Teja, A.S., Vapor-Liquid Critical Properties of Elements and Compounds. 4. Aliphatic Alkanols, J. Chem. Eng. Data, 1995, 40, 1025-1036. [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]

Mejia, Segura, et al., 2010
Mejia, Andres; Segura, Hugo; Cartes, Marcela, Vapor-Liquid Equilibria and Interfacial Tensions of the System Ethanol + 2-Methoxy-2-methylpropane, J. Chem. Eng. Data, 2010, 55, 1, 428-434, https://doi.org/10.1021/je9004068 . [all data]

Aucejo, Loras, et al., 1999
Aucejo, Antonio; Loras, Sonia; Muñoz, Rosa; Ordoñez, Luis Miguel, Isobaric vapor--liquid equilibrium for binary mixtures of 2-methylpentane+ethanol and +2-methyl-2-propanol, Fluid Phase Equilibria, 1999, 156, 1-2, 173-183, https://doi.org/10.1016/S0378-3812(99)00029-1 . [all data]

Diogo, Santos, et al., 1995
Diogo, Hermínio P.; Santos, Rui C.; Nunes, Paulo M.; Minas da Piedade, Manuel E., Ebulliometric apparatus for the measurement of enthalpies of vaporization, Thermochimica Acta, 1995, 249, 113-120, https://doi.org/10.1016/0040-6031(95)90678-9 . [all data]

Ortega, Susial, et al., 1990
Ortega, Juan; Susial, Pedro; De Alfonso, Casiano, Isobaric vapor-liquid equilibrium of methyl butanoate with ethanol and 1-propanol binary systems, J. Chem. Eng. Data, 1990, 35, 2, 216-219, https://doi.org/10.1021/je00060a037 . [all data]

Vine and Wormald, 1989
Vine, M.D.; Wormald, C.J., The enthalpy of ethanol, The Journal of Chemical Thermodynamics, 1989, 21, 11, 1151-1157, https://doi.org/10.1016/0021-9614(89)90101-8 . [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]

Ambrose, Counsell, et al., 1970
Ambrose, D.; Counsell, J.F.; Davenport, A.J., The use of Chebyshev polynomials for the representation of vapour pressures between the triple point and the critical point, The Journal of Chemical Thermodynamics, 1970, 2, 2, 283-294, https://doi.org/10.1016/0021-9614(70)90093-5 . [all data]

Wilhoit and Zwolinski, 1973
Wilhoit, R.C.; Zwolinski, B.J., Physical and thermodynamic properties of aliphatic alcohols, J. Phys. Chem. Ref. Data Suppl., 1973, 1, 2, 1. [all data]

Counsell, Fenwick, et al., 1970
Counsell, J.F.; Fenwick, J.O.; Lees, E.B., Thermodynamic properties of organic oxygen compounds 24. Vapour heat capacities and enthalpies of vaporization of ethanol, 2-methylpropan-1-ol, and pentan-1-ol, The Journal of Chemical Thermodynamics, 1970, 2, 3, 367-372, https://doi.org/10.1016/0021-9614(70)90007-8 . [all data]

Van Ness, Soczek, et al., 1967
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Notes

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