Methyl Alcohol

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Gas phase thermochemistry data

Go To: Top, Condensed phase thermochemistry data, Phase change 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-205. ± 10.kJ/molAVGN/AAverage of 9 values; Individual data points
Quantity Value Units Method Reference Comment
Δcgas-763.68 ± 0.20kJ/molCmRossini, 1932Flame Calorimetry; Corresponding Δfgas = -201.49 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
34.0050.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
36.95100.
38.64150.
39.71200.
42.59273.15
44.06 ± 0.03298.15
44.17300.
51.63400.
59.70500.
67.19600.
73.86700.
79.76800.
84.95900.
89.541000.
93.571100.
97.121200.
100.241300.
102.981400.
105.401500.
110.21750.
113.82000.
116.52250.
118.62500.
120.2750.
121.3000.

Constant pressure heat capacity of gas

Cp,gas (J/mol*K) Temperature (K) Reference Comment
42.4 ± 1.3279.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
48.0 ± 1.3345.6
46.8 ± 1.2347.35
46.1 ± 1.3349.65
47.6 ± 1.2356.55
46.7 ± 1.3358.15
48.2 ± 1.3358.85
48.8 ± 1.3359.85
50.3 ± 1.3368.15
49.0 ± 1.2373.35
51.3 ± 1.3382.15
51.1 ± 1.2398.95
52.3 ± 1.3401.15
51.3 ± 1.2401.35
52.01 ± 0.42403.2
53.2 ± 1.3420.15
53.9 ± 1.2431.45
54.8 ± 1.2442.15
55.9 ± 1.3442.65
56.0 ± 1.2457.35
57.20 ± 0.42464.0
57.8 ± 1.2477.75
58.4 ± 1.2485.05
59.5 ± 1.2498.95
60.4 ± 1.3521.2
61.4 ± 1.2521.35
64.3 ± 1.2555.95
66.4 ± 1.2581.35
66.8 ± 1.2585.35

Condensed phase thermochemistry data

Go To: Top, Gas phase thermochemistry data, Phase change 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-238.4kJ/molCcrBaroody and Carpenter, 1972ALS
Δfliquid-239.5 ± 0.2kJ/molCcbChao and Rossini, 1965see Rossini, 1934; ALS
Δfliquid-238.9 ± 3.6kJ/molCcbGreen, 1960Reanalyzed by Cox and Pilcher, 1970, Original value = -238.5 ± 0.2 kJ/mol; ALS
Δfliquid-250.6kJ/molCcbParks, 1925ALS
Δfliquid-251.3 ± 5.0kJ/molCcbRichards and Davis, 1920DRB
Quantity Value Units Method Reference Comment
Δcliquid-725.7 ± 0.1kJ/molCcbChao and Rossini, 1965see Rossini, 1934; Corresponding Δfliquid = -239.5 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS
Δcliquid-726.5 ± 0.2kJ/molCcbGreen, 1960Corresponding Δfliquid = -238.7 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS
Δcliquid-726.34 ± 0.20kJ/molCcbRossini, 1931Corresponding Δfliquid = -238.83 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS
Δcliquid-715.05kJ/molCcbParks, 1925Corresponding Δfliquid = -250.1 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS
Δcliquid-713.83kJ/molCcbRichards and Davis, 1920At 291 K; Corresponding Δfliquid = -251.34 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS
Quantity Value Units Method Reference Comment
liquid127.19J/mol*KN/ACarlson and Westrum, 1971DH
liquid126.8J/mol*KN/AKelley, 1929DH
liquid129.7J/mol*KN/AParks, Kelley, et al., 1929Extrapolation below 90 K, 34.3 J/mol*K. Revision of previous data.; DH
liquid136.4J/mol*KN/AParks, 1925Extrapolation below 90 K, 40.75 J/mol*K.; DH
Quantity Value Units Method Reference Comment
solid,1 bar1.117J/mol*KN/AAhlberg, Blanchard, et al., 1937DH

Constant pressure heat capacity of liquid

Cp,liquid (J/mol*K) Temperature (K) Reference Comment
79.5298.15Filatov and Afanas'ev, 1992DH
81.11298.15Khasanshin and Zykova, 1989T = 175 to 338 K. Unsmoothed experimental datum.; DH
80.24298.15Andreoli-Ball, Patterson, et al., 1988DH
80.35298.15Okano, Ogawa, et al., 1988DH
81.0298.15Lankford and Criss, 1987DH
81.32298.Korolev, Kukharenko, et al., 1986DH
80.28298.15Ogawa and Murakami, 1986DH
81.56298.15Tanaka, Toyama, et al., 1986DH
80.22298.15Costas and Patterson, 1985T = 298.15, 313.15 K.; DH
81.47298.15Zegers and Somsen, 1984DH
78.90288.15Benson and D'Arcy, 1982DH
81.92298.15Villamanan, Casanova, et al., 1982DH
80.8293.15Atalla, El-Sharkawy, et al., 1981DH
81.13298.15Carlson and Westrum, 1971T = 5 to 332 K.; DH
83.7298.Deshpande and Bhatagadde, 1971T = 298 to 318 K.; DH
85.8313.2Paz Andrade, Paz, et al., 1970DH
85.8298.2Katayama, 1962T = 10 to 60°C.; DH
80.8311.Swietoslawski and Zielenkiewicz, 1960Mean value 21 to 56°C.; DH
86.2323.Hough, Mason, et al., 1950T = 323 to 353 K.; DH
75.77270.Staveley and Gupta, 1949T = 90 to 270 K.; DH
86.6300.8Phillip, 1939DH
83.56313.15Fiock, Ginnings, et al., 1931T = 40 to 110°C.; DH
79.9292.0Kelley, 1929T = 16 to 293 K. Value is unsmoothed experimental datum.; DH
78.2270.Mitsukuri and Hara, 1929T = 190 to 270 K.; DH
79.9290.1Parks, 1925T = 89 to 290 K. Value is unsmoothed experimental datum.; DH
83.3298.von Reis, 1881T = 288 to 335 K.; DH

Constant pressure heat capacity of solid

Cp,solid (J/mol*K) Temperature (K) Reference Comment
68.39120.Sugisaki, Suga, et al., 1968glass phase; T = 20 to 120 K.; DH
5.4020.5Ahlberg, Blanchard, et al., 1937T = 5 to 28 K.; DH
105.173.Maass and Walbauer, 1925T = 93 to 173 K.; DH

Phase change data

Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry 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
Pc81. ± 1.barAVGN/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
Δvap37.6 ± 0.5kJ/molAVGN/AAverage of 11 out of 12 values; Individual data points

Enthalpy of vaporization

ΔvapH (kJ/mol) Temperature (K) Method Reference Comment
35.21337.7N/AMajer and Svoboda, 1985 
39.2258.AStephenson and Malanowski, 1987Based on data from 175. to 273. K.; AC
36.9353.AStephenson and Malanowski, 1987Based on data from 338. to 487. K.; AC
43.7213.AStephenson and Malanowski, 1987Based on data from 188. to 228. K.; AC
38.9275.AStephenson and Malanowski, 1987Based on data from 224. to 290. K.; AC
38.3300.AStephenson and Malanowski, 1987Based on data from 285. to 345. K.; AC
37.0350.AStephenson and Malanowski, 1987Based on data from 335. to 376. K.; AC
36.1388.AStephenson and Malanowski, 1987Based on data from 373. to 458. K.; AC
35.1468.AStephenson and Malanowski, 1987Based on data from 453. to 513. K.; AC
32.7373.CYerlett and Wormald, 1986AC
28.1423.CYerlett and Wormald, 1986AC
20.6473.CYerlett and Wormald, 1986AC
7.4510.CYerlett and Wormald, 1986AC
37.5331.EBCervenkova and Boublik, 1984Based on data from 316. to 336. K.; AC
38.3303.N/AGibbard and Creek, 1974Based on data from 288. to 337. K. See also Boublik, Fried, et al., 1984.; AC
35.2 ± 0.1338.CCounsell and Lee, 1973AC
35.6 ± 0.1331.CCounsell and Lee, 1973AC
36.2 ± 0.1321.CCounsell and Lee, 1973AC
37.0 ± 0.1306.CCounsell and Lee, 1973AC
36.7 ± 0.1313.CSvoboda, Veselý, et al., 1973AC
36.2 ± 0.1323.CSvoboda, Veselý, et al., 1973AC
35.6 ± 0.1333.CSvoboda, Veselý, et al., 1973AC
35.3 ± 0.1338.CSvoboda, Veselý, et al., 1973AC
34.7 ± 0.1343.CSvoboda, Veselý, et al., 1973AC
37.0352.N/AWilhoit and Zwolinski, 1973Based on data from 337. to 383. K.; AC
38.7290.EBBoublík and Aim, 1972Based on data from 275. to 336. K. See also Stephenson and Malanowski, 1987.; AC
38.3303.EBAmbrose and Sprake, 1970Based on data from 288. to 357. K.; AC
36.3368.N/AHirata, Suda, et al., 1967Based on data from 353. to 483. K.; AC
38.4293.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) (kJ/mol)
    Tr = reduced temperature (T / Tc)

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Temperature (K) 298. to 477.
A (kJ/mol) 45.3
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 (bar)
    T = temperature (K)

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Temperature (K) A B C Reference Comment
353.5 to 512.635.158531569.613-34.846Ambrose, Sprake, et al., 1975Coefficents calculated by NIST from author's data.
288.1 to 356.835.204091581.341-33.50Ambrose and Sprake, 1970Coefficents calculated by NIST from author's data.
353. to 483.5.313011676.569-21.728Hirata and Suda, 1967Coefficents calculated by NIST from author's data.

Enthalpy of fusion

ΔfusH (kJ/mol) Temperature (K) Reference Comment
3.18175.3Domalski and Hearing, 1996AC
2.196176.Maass and Walbauer, 1925DH

Entropy of fusion

ΔfusS (J/mol*K) Temperature (K) Reference Comment
12.5176.Maass and Walbauer, 1925DH

Entropy of fusion

ΔfusS (J/mol*K) Temperature (K) Reference Comment
3.7161.1Domalski and Hearing, 1996CAL
18.1175.3
4.0157.3
18.3175.6

Enthalpy of phase transition

ΔHtrs (kJ/mol) Temperature (K) Initial Phase Final Phase Reference Comment
0.6360157.34crystaline, IIcrystaline, ICarlson and Westrum, 1971DH
3.2154175.59crystaline, IliquidCarlson and Westrum, 1971DH
1.540103.crystalineglassSugisaki, Suga, et al., 1968Glass transition.; DH
0.711157.8crystaline, IIcrystaline, IStaveley and Gupta, 1949DH
3.159175.4crystaline, IliquidStaveley and Gupta, 1949DH
0.6456157.4crystaline, IIcrystaline, IKelley, 1929DH
3.167175.2crystaline, IliquidKelley, 1929DH
0.590161.1crystaline, IIcrystaline, IParks, 1925DH
3.176175.3crystaline, IliquidParks, 1925DH

Entropy of phase transition

ΔStrs (J/mol*K) Temperature (K) Initial Phase Final Phase Reference Comment
4.04157.34crystaline, IIcrystaline, ICarlson and Westrum, 1971DH
18.31175.59crystaline, IliquidCarlson and Westrum, 1971DH
14.95103.crystalineglassSugisaki, Suga, et al., 1968Glass; DH
4.51157.8crystaline, IIcrystaline, IStaveley and Gupta, 1949DH
18.01175.4crystaline, IliquidStaveley and Gupta, 1949DH
4.10157.4crystaline, IIcrystaline, IKelley, 1929DH
18.08175.2crystaline, IliquidKelley, 1929DH
3.66161.1crystaline, IIcrystaline, IParks, 1925DH
18.12175.3crystaline, 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:


References

Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change 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
Chao, J.; Rossini, F.D., Heats of combustion, formation, and isomerization of nineteen alkanols, J. Chem. Eng. Data, 1965, 10, 374-379. [all data]

Rossini, 1934
Rossini, F.D., Heats of combustion and of formation of the normal aliphatic alcohols in the gaseous and liquid states, and the energies of their atomic linkages, J. Res. NBS, 1934, 13, 189-197. [all data]

Green, 1960
Green, J.H.S., Revision of the values of the heats of formation of normal alcohols, Chem. Ind. (London), 1960, 1215-1216. [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]

Parks, 1925
Parks, G.S., Thermal data on organic compounds I. The heat capacities and free energies of methyl, ethyl and normal-butyl alcohols, J. Am. Chem. Soc., 1925, 47, 338-345. [all data]

Richards and Davis, 1920
Richards, T.W.; Davis, H.S., The heats of combustion of benzene, toluene, aliphatic alcohols, cyclohexanol, and other carbon compounds, J. Am. Chem. Soc., 1920, 42, 1599-1617. [all data]

Rossini, 1931
Rossini, F.D., The heat of combustion of methyl alcohol, Proc. Nat'l Acad. Sci., 1931, 17, 343-347. [all data]

Carlson and Westrum, 1971
Carlson, H.G.; Westrum, E.F., Jr., Methanol: heat capacity, enthalpies of transition and melting, and thermodynamic properties from 5-300K, J. Chem. Phys., 1971, 54, 1464-1471. [all data]

Kelley, 1929
Kelley, K.K., The heat capacity of methyl alcohol from 16K to 298K and the corresponding entropy and free energy, J. Am. Chem. Soc., 1929, 51, 180-187. [all data]

Parks, Kelley, et al., 1929
Parks, G.S.; Kelley, K.K.; Huffman, H.M., Thermal data on organic compounds. V. A revision of the entropies and free energies of nineteen organic compounds, J. Am. Chem. Soc., 1929, 51, 1969-1973. [all data]

Ahlberg, Blanchard, et al., 1937
Ahlberg, J.E.; Blanchard, E.R.; Lundberg, W.O., The heat capacities of benzene, methyl alcohol and glycerol at very low temperatures, J. Chem. Phys., 1937, 5, 537-551. [all data]

Filatov and Afanas'ev, 1992
Filatov, V.A.; Afanas'ev, V.N., Differential heat-flux calorimeter, Izv. Vysshikh. Uchebn. Zaved., Khim. Khim. Tekhnol., 1992, 35(8), 97-100. [all data]

Khasanshin and Zykova, 1989
Khasanshin, T.S.; Zykova, T.B., Specific heat of saturated monatomic alcohols, Inzh. -Fiz. Zhur., 1989, 56(6), 991-994. [all data]

Andreoli-Ball, Patterson, et al., 1988
Andreoli-Ball, L.; Patterson, D.; Costas, M.; Caceres-Alonso, M., Heat capacity and corresponding states in alkan-1-ol-n-alkane systems, J. Chem. Soc., Faraday Trans. 1, 1988, 84(11), 3991-4012. [all data]

Okano, Ogawa, et al., 1988
Okano, T.; Ogawa, H.; Murakami, S., Molar excess volumes, isentropic compressions, and isobaric heat capacities of methanol-isomeric butanol systems at 298.15 K, Can. J. Chem., 1988, 66, 713-717. [all data]

Lankford and Criss, 1987
Lankford, J.I.; Criss, C.M., Partial molar heat caqpacities of selected electrolytes and benzene in methanol and dimethyldulfoxide at 25, 40 and 80°C, J. Solution Chem., 1987, 16(11), 885-906. [all data]

Korolev, Kukharenko, et al., 1986
Korolev, V.P.; Kukharenko, V.A.; Krestov, G.A., Specific heat of binary mixtures of aliphatic alcohols with N,N-dimethylformamide and dimethylsulphoxide, Zhur. Fiz. Khim., 1986, 60, 1854-1857. [all data]

Ogawa and Murakami, 1986
Ogawa, H.; Murakami, S., Excess isobaric heat capacities for water + alkanol mixtures at 298.15 K, Thermochim. Acta, 1986, 109, 145-154. [all data]

Tanaka, Toyama, et al., 1986
Tanaka, R.; Toyama, S.; Murakami, S., Heat capacities of {xCnH2n+1OH+(1-x)C7H16} for n = 1 to 6 at 298.15 K, J. Chem. Thermodynam., 1986, 18, 63-73. [all data]

Costas and Patterson, 1985
Costas, M.; Patterson, D., Self-association of alcohols in inert solvents, J. Chem. Soc., Faraday Trans. 1, 1985, 81, 635-654. [all data]

Zegers and Somsen, 1984
Zegers, H.C.; Somsen, G., Partial molar volumes and heat capacities in (dimethylformamide + an n-alkanol), J. Chem. Thermodynam., 1984, 16, 225-235. [all data]

Benson and D'Arcy, 1982
Benson, G.C.; D'Arcy, P.J., Excess isobaric heat capacities of water - n-alcohol mixtures, J. Chem. Eng. Data, 1982, 27, 439-442. [all data]

Villamanan, Casanova, et al., 1982
Villamanan, M.A.; Casanova, C.; Roux-Desgranges, G.; Grolier, J.-P.E., Thermochemical behavior of mixtures of n-alcohol + aliphatic ether: heat capacities and volumes at 298.15 K, Thermochim. Acta, 1982, 52, 279-283. [all data]

Atalla, El-Sharkawy, et al., 1981
Atalla, S.R.; El-Sharkawy, A.A.; Gasser, F.A., Measurement of thermal properties of liquids with an AC heated-wire technique, Inter. J. Thermophys., 1981, 2(2), 155-162. [all data]

Deshpande and Bhatagadde, 1971
Deshpande, D.D.; Bhatagadde, L.G., Heat capacities at constant volume, free volumes, and rotational freedom in some liquids, Aust. J. Chem., 1971, 24, 1817-1822. [all data]

Paz Andrade, Paz, et al., 1970
Paz Andrade, M.I.; Paz, J.M.; Recacho, E., Contribucion a la microcalorimetria de los calores especificos de solidos y liquidos, An. Quim., 1970, 66, 961-967. [all data]

Katayama, 1962
Katayama, T., Heats of mixing, liquid heat capacities and enthalpy, concentration charts for methanol-water and isopropanol-water systems, Kagaku Kogaku, 1962, 26, 361-372. [all data]

Swietoslawski and Zielenkiewicz, 1960
Swietoslawski, W.; Zielenkiewicz, A., Mean specific heat in homologous series of binary and ternary positive azeotropes, Bull. Acad. Pol. Sci. Ser. Sci. Chim., 1960, 8, 651-653. [all data]

Hough, Mason, et al., 1950
Hough, E.W.; Mason, D.M.; Sage, B.H., Heat capacities of several organic liquids, J. Am. Chem. Soc., 1950, 72, 5775-5777. [all data]

Staveley and Gupta, 1949
Staveley, L.A.K.; Gupta, A.K., A semi-micro low-temperature calorimeter, and a comparison of some thermodynamic properties of methyl alcohol and methyl deuteroxide, Trans. Faraday Soc., 1949, 45, 50-61. [all data]

Phillip, 1939
Phillip, N.M., Adiabatic and isothermal compressibilities of liquids, Proc. Indian Acad. Sci., 1939, A9, 109-120. [all data]

Fiock, Ginnings, et al., 1931
Fiock, E.F.; Ginnings, D.C.; Holton, W.B., Calorimetric determinations of thermal properties of methyl alcohol, ethyl alcohol, and benzene, J. Res., 1931, NBS 6, 881-900. [all data]

Mitsukuri and Hara, 1929
Mitsukuri, S.; Hara, K., Specific heats of acetone, methyl-, ethyl-, and n-propyl-alcohols at low temperatures, Bull. Chem. Soc. Japan, 1929, 4, 77-81. [all data]

von Reis, 1881
von Reis, M.A., Die specifische Wärme flüssiger organischer Verbindungen und ihre Beziehung zu deren Moleculargewicht, Ann. Physik [3], 1881, 13, 447-464. [all data]

Sugisaki, Suga, et al., 1968
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Notes

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