Methyl Alcohol

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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
DRB - Donald R. Burgess, Jr.
GT - Glushko Thermocenter, Russian Academy of Sciences, Moscow

Quantity Value Units Method Reference Comment
Δfgas-49. ± 3.kcal/molAVGN/AAverage of 9 values; Individual data points
Quantity Value Units Method Reference Comment
Δcgas-182.52 ± 0.048kcal/molCmRossini, 1932Flame Calorimetry; Corresponding Δfgas = -48.157 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS

Constant pressure heat capacity of gas

Cp,gas (cal/mol*K) Temperature (K) Reference Comment
8.12650.Thermodynamics Research Center, 1997p=1 bar. Recommended entropies and heat capacities are in good agreement with other statistically calculated values [ Ivash E.V., 1955, Zhuravlev E.Z., 1959, Chen S.S., 1977, Chao J., 1986, Gurvich, Veyts, et al., 1989]. Please also see Chao J., 1986, 2.; GT
8.831100.
9.235150.
9.491200.
10.18273.15
10.53 ± 0.007298.15
10.56300.
12.34400.
14.27500.
16.06600.
17.65700.
19.06800.
20.30900.
21.401000.
22.361100.
23.211200.
23.9581300.
24.6131400.
25.1911500.
26.341750.
27.202000.
27.842250.
28.352500.
28.72750.
28.93000.

Constant pressure heat capacity of gas

Cp,gas (cal/mol*K) Temperature (K) Reference Comment
10.13 ± 0.30279.Stromsoe E., 1970Heat capacity at 279 K was obtained by thermal conductivity [ Halford J.O., 1957]. Vapor heat capacities from calorimetric measurements [ De Vries T., 1941] were converted to the ideal gas heat capacities by corrections for the gas imperfection effects [ Chen S.S., 1977, Chao J., 1986, 2]. 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 1.17 J/mol*K. The accuracy of the experimental heat capacities [ Stromsoe E., 1970] is estimated as less than 0.3%. Please also see De Vries T., 1941, Weltner W., 1951, Halford J.O., 1957.; GT
11.46 ± 0.30345.6
11.19 ± 0.28347.35
11.01 ± 0.30349.65
11.37 ± 0.28356.55
11.17 ± 0.30358.15
11.52 ± 0.30358.85
11.67 ± 0.30359.85
12.02 ± 0.30368.15
11.71 ± 0.28373.35
12.26 ± 0.30382.15
12.22 ± 0.28398.95
12.51 ± 0.30401.15
12.27 ± 0.28401.35
12.43 ± 0.10403.2
12.72 ± 0.30420.15
12.88 ± 0.28431.45
13.09 ± 0.28442.15
13.36 ± 0.30442.65
13.39 ± 0.28457.35
13.67 ± 0.10464.0
13.80 ± 0.28477.75
13.95 ± 0.28485.05
14.23 ± 0.28498.95
14.44 ± 0.30521.2
14.68 ± 0.28521.35
15.37 ± 0.28555.95
15.88 ± 0.28581.35
15.96 ± 0.28585.35

Condensed phase thermochemistry data

Go To: Top, Gas 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
DRB - Donald R. Burgess, Jr.
DH - Eugene S. Domalski and Elizabeth D. Hearing

Quantity Value Units Method Reference Comment
Δfliquid-56.97kcal/molCcrBaroody and Carpenter, 1972ALS
Δfliquid-57.24 ± 0.04kcal/molCcbChao and Rossini, 1965see Rossini, 1934; ALS
Δfliquid-57.10 ± 0.86kcal/molCcbGreen, 1960Reanalyzed by Cox and Pilcher, 1970, Original value = -57.01 ± 0.05 kcal/mol; ALS
Δfliquid-59.89kcal/molCcbParks, 1925ALS
Δfliquid-60.1 ± 1.2kcal/molCcbRichards and Davis, 1920DRB
Quantity Value Units Method Reference Comment
Δcliquid-173.45 ± 0.03kcal/molCcbChao and Rossini, 1965see Rossini, 1934; Corresponding Δfliquid = -57.23 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS
Δcliquid-173.64 ± 0.05kcal/molCcbGreen, 1960Corresponding Δfliquid = -57.04 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS
Δcliquid-173.60 ± 0.048kcal/molCcbRossini, 1931Corresponding Δfliquid = -57.082 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS
Δcliquid-170.90kcal/molCcbParks, 1925Corresponding Δfliquid = -59.78 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS
Δcliquid-170.61kcal/molCcbRichards and Davis, 1920At 291 K; Corresponding Δfliquid = -60.072 kcal/mol (simple calculation by NIST; no Washburn corrections); ALS
Quantity Value Units Method Reference Comment
liquid30.399cal/mol*KN/ACarlson and Westrum, 1971DH
liquid30.31cal/mol*KN/AKelley, 1929DH
liquid31.00cal/mol*KN/AParks, Kelley, et al., 1929Extrapolation below 90 K, 34.3 J/mol*K. Revision of previous data.; DH
liquid32.60cal/mol*KN/AParks, 1925Extrapolation below 90 K, 40.75 J/mol*K.; DH
Quantity Value Units Method Reference Comment
solid,1 bar0.2670cal/mol*KN/AAhlberg, Blanchard, et al., 1937DH

Constant pressure heat capacity of liquid

Cp,liquid (cal/mol*K) Temperature (K) Reference Comment
19.0298.15Filatov and Afanas'ev, 1992DH
19.39298.15Khasanshin and Zykova, 1989T = 175 to 338 K. Unsmoothed experimental datum.; DH
19.18298.15Andreoli-Ball, Patterson, et al., 1988DH
19.20298.15Okano, Ogawa, et al., 1988DH
19.4298.15Lankford and Criss, 1987DH
19.44298.Korolev, Kukharenko, et al., 1986DH
19.19298.15Ogawa and Murakami, 1986DH
19.49298.15Tanaka, Toyama, et al., 1986DH
19.17298.15Costas and Patterson, 1985T = 298.15, 313.15 K.; DH
19.47298.15Zegers and Somsen, 1984DH
18.86288.15Benson and D'Arcy, 1982DH
19.58298.15Villamanan, Casanova, et al., 1982DH
19.3293.15Atalla, El-Sharkawy, et al., 1981DH
19.39298.15Carlson and Westrum, 1971T = 5 to 332 K.; DH
20.0298.Deshpande and Bhatagadde, 1971T = 298 to 318 K.; DH
20.5313.2Paz Andrade, Paz, et al., 1970DH
20.5298.2Katayama, 1962T = 10 to 60°C.; DH
19.3311.Swietoslawski and Zielenkiewicz, 1960Mean value 21 to 56°C.; DH
20.6323.Hough, Mason, et al., 1950T = 323 to 353 K.; DH
18.11270.Staveley and Gupta, 1949T = 90 to 270 K.; DH
20.7300.8Phillip, 1939DH
19.97313.15Fiock, Ginnings, et al., 1931T = 40 to 110°C.; DH
19.1292.0Kelley, 1929T = 16 to 293 K. Value is unsmoothed experimental datum.; DH
18.7270.Mitsukuri and Hara, 1929T = 190 to 270 K.; DH
19.1290.1Parks, 1925T = 89 to 290 K. Value is unsmoothed experimental datum.; DH
19.9298.von Reis, 1881T = 288 to 335 K.; DH

Constant pressure heat capacity of solid

Cp,solid (cal/mol*K) Temperature (K) Reference Comment
16.35120.Sugisaki, Suga, et al., 1968glass phase; T = 20 to 120 K.; DH
1.2920.5Ahlberg, Blanchard, et al., 1937T = 5 to 28 K.; DH
25.1173.Maass and Walbauer, 1925T = 93 to 173 K.; DH

Phase change data

Go To: Top, Gas phase thermochemistry data, 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:
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, Chris Muzny director
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
Tboil337.8 ± 0.3KAVGN/AAverage of 154 out of 171 values; Individual data points
Quantity Value Units Method Reference Comment
Tfus176. ± 1.KAVGN/AAverage of 13 values; Individual data points
Quantity Value Units Method Reference Comment
Ttriple175.5 ± 0.5KAVGN/AAverage of 8 values; Individual data points
Quantity Value Units Method Reference Comment
Tc513. ± 1.KAVGN/AAverage of 27 out of 31 values; Individual data points
Quantity Value Units Method Reference Comment
Pc79. ± 1.atmAVGN/AAverage of 17 out of 20 values; Individual data points
Quantity Value Units Method Reference Comment
Vc0.117l/molN/AGude and Teja, 1995 
Vc0.113024l/molN/ACraven and de Reuck, 1986TRC
Vc0.118l/molN/AFrancesconi, Lentz, et al., 1981Uncertainty assigned by TRC = 0.004 l/mol; TRC
Vc0.11663l/molN/AZubarev and Bagdonas, 1969Uncertainty assigned by TRC = 0.0035 l/mol; TRC
Quantity Value Units Method Reference Comment
ρc8.51 ± 0.07mol/lAVGN/AAverage of 7 values; Individual data points
Quantity Value Units Method Reference Comment
Δvap9.0 ± 0.1kcal/molAVGN/AAverage of 11 out of 12 values; Individual data points

Enthalpy of vaporization

ΔvapH (kcal/mol) Temperature (K) Method Reference Comment
8.415337.7N/AMajer and Svoboda, 1985 
9.37258.AStephenson and Malanowski, 1987Based on data from 175. to 273. K.; AC
8.82353.AStephenson and Malanowski, 1987Based on data from 338. to 487. K.; AC
10.4213.AStephenson and Malanowski, 1987Based on data from 188. to 228. K.; AC
9.30275.AStephenson and Malanowski, 1987Based on data from 224. to 290. K.; AC
9.15300.AStephenson and Malanowski, 1987Based on data from 285. to 345. K.; AC
8.84350.AStephenson and Malanowski, 1987Based on data from 335. to 376. K.; AC
8.63388.AStephenson and Malanowski, 1987Based on data from 373. to 458. K.; AC
8.39468.AStephenson and Malanowski, 1987Based on data from 453. to 513. K.; AC
7.82373.CYerlett and Wormald, 1986AC
6.72423.CYerlett and Wormald, 1986AC
4.92473.CYerlett and Wormald, 1986AC
1.8510.CYerlett and Wormald, 1986AC
8.96331.EBCervenkova and Boublik, 1984Based on data from 316. to 336. K.; AC
9.15303.N/AGibbard and Creek, 1974Based on data from 288. to 337. K. See also Boublik, Fried, et al., 1984.; AC
8.41 ± 0.02338.CCounsell and Lee, 1973AC
8.51 ± 0.02331.CCounsell and Lee, 1973AC
8.65 ± 0.02321.CCounsell and Lee, 1973AC
8.84 ± 0.02306.CCounsell and Lee, 1973AC
8.77 ± 0.02313.CSvoboda, Veselý, et al., 1973AC
8.65 ± 0.02323.CSvoboda, Veselý, et al., 1973AC
8.51 ± 0.02333.CSvoboda, Veselý, et al., 1973AC
8.44 ± 0.02338.CSvoboda, Veselý, et al., 1973AC
8.29 ± 0.02343.CSvoboda, Veselý, et al., 1973AC
8.84352.N/AWilhoit and Zwolinski, 1973Based on data from 337. to 383. K.; AC
9.25290.EBBoublík and Aim, 1972Based on data from 275. to 336. K. See also Stephenson and Malanowski, 1987.; AC
9.15303.EBAmbrose and Sprake, 1970Based on data from 288. to 357. K.; AC
8.68368.N/AHirata, Suda, et al., 1967Based on data from 353. to 483. K.; AC
9.18293.N/AKlyueva, Mischenko, et al., 1960Based on data from 278. to 323. K.; AC

Enthalpy of vaporization

ΔvapH = A exp(-αTr) (1 − Tr)β
    ΔvapH = Enthalpy of vaporization (at saturation pressure) (kcal/mol)
    Tr = reduced temperature (T / Tc)

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Temperature (K) 298. to 477.
A (kcal/mol) 10.8
α -0.31
β 0.4241
Tc (K) 512.6
ReferenceMajer and Svoboda, 1985

Antoine Equation Parameters

log10(P) = A − (B / (T + C))
    P = vapor pressure (atm)
    T = temperature (K)

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Temperature (K) A B C Reference Comment
353.5 to 512.635.152821569.613-34.846Ambrose, Sprake, et al., 1975Coefficents calculated by NIST from author's data.
288.1 to 356.835.198381581.341-33.50Ambrose and Sprake, 1970Coefficents calculated by NIST from author's data.
353. to 483.5.307301676.569-21.728Hirata and Suda, 1967Coefficents calculated by NIST from author's data.

Enthalpy of fusion

ΔfusH (kcal/mol) Temperature (K) Reference Comment
0.760175.3Domalski and Hearing, 1996AC
0.5249176.Maass and Walbauer, 1925DH

Entropy of fusion

ΔfusS (cal/mol*K) Temperature (K) Reference Comment
2.99176.Maass and Walbauer, 1925DH

Entropy of fusion

ΔfusS (cal/mol*K) Temperature (K) Reference Comment
0.88161.1Domalski and Hearing, 1996CAL
4.33175.3
0.96157.3
4.37175.6

Enthalpy of phase transition

ΔHtrs (kcal/mol) Temperature (K) Initial Phase Final Phase Reference Comment
0.1520157.34crystaline, IIcrystaline, ICarlson and Westrum, 1971DH
0.76850175.59crystaline, IliquidCarlson and Westrum, 1971DH
0.3681103.crystalineglassSugisaki, Suga, et al., 1968Glass transition.; DH
0.170157.8crystaline, IIcrystaline, IStaveley and Gupta, 1949DH
0.7550175.4crystaline, IliquidStaveley and Gupta, 1949DH
0.1543157.4crystaline, IIcrystaline, IKelley, 1929DH
0.7569175.2crystaline, IliquidKelley, 1929DH
0.141161.1crystaline, IIcrystaline, IParks, 1925DH
0.7591175.3crystaline, IliquidParks, 1925DH

Entropy of phase transition

ΔStrs (cal/mol*K) Temperature (K) Initial Phase Final Phase Reference Comment
0.966157.34crystaline, IIcrystaline, ICarlson and Westrum, 1971DH
4.376175.59crystaline, IliquidCarlson and Westrum, 1971DH
3.573103.crystalineglassSugisaki, Suga, et al., 1968Glass; DH
1.08157.8crystaline, IIcrystaline, IStaveley and Gupta, 1949DH
4.304175.4crystaline, IliquidStaveley and Gupta, 1949DH
0.980157.4crystaline, IIcrystaline, IKelley, 1929DH
4.321175.2crystaline, IliquidKelley, 1929DH
0.875161.1crystaline, IIcrystaline, IParks, 1925DH
4.331175.3crystaline, IliquidParks, 1925DH

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

Go To: Top, Gas phase thermochemistry data, 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) = H exp(d(ln(kH))/d(1/T) ((1/T) - 1/(298.15 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)

H (mol/(kg*bar)) d(ln(kH))/d(1/T) (K) Method Reference Comment
140. QN/A missing citation give several references for the Henry's law constants but don't assign them to specific species.
220. XN/A 
220.5200.MN/A 
220. XN/AValue given here as quoted by missing citation.
160.5600.XN/A 
230. MN/A 
210. M,XTimmermans, 1960Value given here as quoted by missing citation.
230. MButler, Ramchandani, et al., 1935This paper supersedes earlier work with more concentrated solutions Butler, Thomson, et al., 1933.

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
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 CH4O+ (ion structure unspecified)

Quantity Value Units Method Reference Comment
IE (evaluated)10.84 ± 0.01eVN/AN/AL
Quantity Value Units Method Reference Comment
Proton affinity (review)180.3kcal/molN/AHunter and Lias, 1998HL
Quantity Value Units Method Reference Comment
Gas basicity173.2kcal/molN/AHunter and Lias, 1998HL

Ionization energy determinations

IE (eV) Method Reference Comment
10.85 ± 0.03PITao, Klemm, et al., 1992LL
10.82 ± 0.05EIHolmes and Lossing, 1991LL
10.84 ± 0.07EIBowen and Maccoll, 1984LBLHLM
10.9EIMishchanchuk, Pokrovskii, et al., 1982LBLHLM
10.84 ± 0.08EIAllam, Migahed, et al., 1982LBLHLM
10.90 ± 0.03EISahini, Constantin, et al., 1978LLK
10.85 ± 0.01PIBerkowitz, 1978LLK
10.846 ± 0.002PEMacNeil and Dixon, 1977LLK
10.90 ± 0.12EIFinney and Harrison, 1972LLK
10.83 ± 0.03PIWarneck, 1971LLK
10.85 ± 0.02PECocksey, Eland, et al., 1971LLK
10.85PEBaker, Betteridge, et al., 1971LLK
10.85PEBaker, Betteridge, et al., 1971LLK
10.829 ± 0.015PIOmura, Kaneko, et al., 1969RDSH
10.85EILifshitz, Shapiro, et al., 1969RDSH
10.83PEDewar and Worley, 1969RDSH
10.84 ± 0.02PIRefaey and Chupka, 1968RDSH
10.85CICermak, 1968RDSH
10.83PEAl-Joboury and Turner, 1964RDSH
10.85 ± 0.02PIWatanabe, 1954RDSH
10.96EIVorob'ev, Furlei, et al., 1989Vertical value; LL
11.0PEVon Niessen, Bieri, et al., 1980Vertical value; LLK
10.95PEUtsunomiya, Kobayashi, et al., 1980Vertical value; LLK
10.95PEKobayashi, 1978Vertical value; LLK
10.86PEBenoit and Harrison, 1977Vertical value; LLK
10.97 ± 0.03PEPeel and Willett, 1975Vertical value; LLK
10.96PERobin and Kuebler, 1973Vertical value; LLK
10.95PEOgata, Onizuka, et al., 1973Vertical value; LLK
10.94PEKatsumata, Iwai, et al., 1973Vertical value; LLK
10.95PEOgata, Onizuka, et al., 1972Vertical value; LLK
10.96PEBaker, Betteridge, et al., 1971Vertical value; LLK

Appearance energy determinations

Ion AE (eV) Other Products MethodReferenceComment
CH+22.31 ± 0.09?EIReed and Snedden, 1956RDSH
CHO+13.06 ± 0.10H2+HPIWarneck, 1971LLK
CHO+14.0 ± 0.2H2+HEILifshitz, Shapiro, et al., 1969RDSH
CH2+14.05 ± 0.05H2OPIWarneck, 1971LLK
CH2+15.3H2OEIHaney and Franklin, 1968RDSH
CH2O+10.9H2EIMishchanchuk, Pokrovskii, et al., 1982LBLHLM
CH2O+12.05 ± 0.12H2PIWarneck, 1971LLK
CH2O+12.45H2PIRefaey and Chupka, 1968RDSH
CH3+13.82 ± 0.04OHPIWarneck, 1971LLK
CH3+13.5OHEIFriedman, Long, et al., 1957RDSH
CH3O+11.67 ± 0.09HEIBowen and Maccoll, 1984LBLHLM
CH3O+10.4HEIMishchanchuk, Pokrovskii, et al., 1982LBLHLM
CH3O+11.85 ± 0.08HEIAllam, Migahed, et al., 1982LBLHLM
CH3O+11.88 ± 0.05HEISelim and Helal, 1981LLK
CH3O+11.69HEILossing, 1977LLK
CH3O+11.76 ± 0.11HEIFinney and Harrison, 1972LLK
CH3O+11.55 ± 0.03HPIWarneck, 1971LLK
CH3O+11.66 ± 0.04HPIOmura, Kaneko, et al., 1969RDSH
CH3O+11.67HEILifshitz, Shapiro, et al., 1969RDSH
CH3O+11.67 ± 0.03HPIRefaey and Chupka, 1968RDSH
CH3O+[CH2OH+]11.649 ± 0.003HPIBerkowitz, Ellison, et al., 1994Unpublished results of B. Ruscic and J. Berkowitz; LL
CO+13.72H2EIFriedman, Long, et al., 1957RDSH
CO+14.31 ± 0.052H2EIFriedland and Strakna, 1956RDSH

De-protonation reactions

CH3O- + Hydrogen cation = Methyl Alcohol

By formula: CH3O- + H+ = CH4O

Quantity Value Units Method Reference Comment
Δr382. ± 2.kcal/molAVGN/AAverage of 6 values; Individual data points
Quantity Value Units Method Reference Comment
Δr376.02 ± 0.62kcal/molH-TSNee, Osterwalder, et al., 2006gas phase; B
Δr376.04 ± 0.55kcal/molH-TSOsborn, Leahy, et al., 1998gas phase; B
Δr374.0 ± 2.0kcal/molIMREBartmess, Scott, et al., 1979gas phase; The acidity is 1.2 kcal/mol stronger than that from the D-EA cycle, due to the multi-compound fit for the acidity scale.; value altered from reference due to change in acidity scale; B
Δr374.6 ± 2.1kcal/molH-TSHaas and Harrison, 1993gas phase; Both metastable and 50 eV collision energy.; B
Δr375.10 ± 0.60kcal/molTDEqMeot-ner and Sieck, 1986gas phase; Experimental entropy: 21.5 eu, 0.6 less than H2O; 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.

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]

Ivash E.V., 1955
Ivash E.V., Thermodynamic properties of ideal gaseous methanol, J. Chem. Phys., 1955, 23, 1814-1818. [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]

Chen S.S., 1977
Chen S.S., Thermodynamic properties of normal and deuterated methanols, J. Phys. Chem. Ref. Data, 1977, 6, 105-112. [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]

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]

De Vries T., 1941
De Vries T., The heat capacity of organic vapors. I. Methyl alcohol, J. Am. Chem. Soc., 1941, 63, 1343-1346. [all data]

Weltner W., 1951
Weltner W., Jr., Methyl alcohol: the entropy, heat capacity and polymerization equilibria in the vapor, and potential barrier to internal rotation, J. Am. Chem. Soc., 1951, 73, 2606-2610. [all data]

Baroody and Carpenter, 1972
Baroody, E.E.; Carpenter, G.A., Heats of formation of propellant compounds (U), Rpt. Naval Ordnance Systems Command Task No. 331-003/067-1/UR2402-001 for Naval Ordance Station, Indian Head, MD, 1972, 1-9. [all data]

Chao and Rossini, 1965
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Notes

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