1-Propanol, 2-methyl-

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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:
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-283.8 ± 0.9kJ/molEqkConnett, 1975Heat of dehydrogenation; ALS
Δfgas-282.9kJ/molN/AChao and Rossini, 1965Value computed using ΔfHliquid° value of -333.6±0.6 kj/mol from Chao and Rossini, 1965 and ΔvapH° value of 50.7 kj/mol from Skinner and Snelson, 1960.; DRB
Δfgas-284. ± 1.5kJ/molCcbSkinner and Snelson, 1960ALS
Quantity Value Units Method Reference Comment
gas350.0J/mol*KN/ACounsell J.F., 1968GT

Constant pressure heat capacity of gas

Cp,gas (J/mol*K) Temperature (K) Reference Comment
133.74379.99Stromsoe E., 1970Ideal 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 0.71 J/mol*K. The accuracy of the experimental heat capacities [ Stromsoe E., 1970] is estimated as less than 0.3%. Please also see Counsell J.F., 1970.; GT
134.34381.23
140.10 ± 0.71390.55
141.76 ± 0.71397.65
139.55400.03
143.92 ± 0.71406.95
146.25 ± 0.71416.95
147.91 ± 0.71424.05
146.35425.01
152.05 ± 0.71441.85
152.97450.06
154.24 ± 0.71451.25
159.62 ± 0.71474.35
158.94475.09
160.41 ± 0.71477.75
165.96 ± 0.71501.55
171.62 ± 0.71525.85
176.39 ± 0.71546.35
184.92 ± 0.71582.95
189.48 ± 0.71602.55

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
Δfliquid-334.6 ± 0.9kJ/molEqkConnett, 1975Heat of dehydrogenation; ALS
Δfliquid-333.6 ± 0.63kJ/molCcbChao and Rossini, 1965see Rossini, 1934; ALS
Δfliquid-334.7 ± 0.84kJ/molCcbSkinner and Snelson, 1960ALS
Quantity Value Units Method Reference Comment
Δcliquid-2669.6 ± 0.59kJ/molCcbChao and Rossini, 1965see Rossini, 1934; Corresponding Δfliquid = -333.5 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS
Δcliquid-2668.5 ± 0.84kJ/molCcbSkinner and Snelson, 1960Corresponding Δfliquid = -334.7 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS
Δcliquid-2665.79kJ/molCcbRichards and Davis, 1920At 291 K; Corresponding Δfliquid = -337.40 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS
Quantity Value Units Method Reference Comment
liquid214.5J/mol*KN/ACounsell, Lees, et al., 1968DH
Quantity Value Units Method Reference Comment
solid,1 bar140.7J/mol*KN/ACounsell, Lees, et al., 1968glass phase; DH

Constant pressure heat capacity of liquid

Cp,liquid (J/mol*K) Temperature (K) Reference Comment
181.05298.15Okano, Ogawa, et al., 1988DH
182.01298.15Piekarski and Somsen, 1988DH
185.6303.15Rybalkin, Emel'yanov, et al., 1978T = 293.15 to 353.15 K. Cp given as 2504 J/kg*K.; DH
185.4301.2Paz Andrade, Paz, et al., 1970T = 28, 40°C.; DH
181.0298.15Counsell, Lees, et al., 1968T = 10 to 350 K.; DH
201.3323.Swietoslawski and Zielenkiewicz, 1960Mean value 21 to 78°C.; DH
215.1333.Swietoslawski and Zielenkiewicz, 1958Mean value 21 to 99°C.; DH
184.1298.1Zhdanov, 1941T = 5 to 46°C.; DH
187.0303.Willams and Daniels, 1924T = 303 to 343 K. Equation only.; DH

Constant pressure heat capacity of solid

Cp,solid (J/mol*K) Temperature (K) Reference Comment
129.2180.Counsell, Lees, et al., 1968glass phase; T = 10 to 180 K.; 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
Tboil380.8 ± 0.9KAVGN/AAverage of 77 out of 89 values; Individual data points
Quantity Value Units Method Reference Comment
Tfus165.15KN/AAnonymous, 1958TRC
Tfus169.KN/AKanda, Otsubo, et al., 1950Uncertainty assigned by TRC = 2. K; TRC
Quantity Value Units Method Reference Comment
Ttriple171.2KN/AWilhoit, Chao, et al., 1985Uncertainty assigned by TRC = 0.01 K; TRC
Ttriple171.18KN/ACounsell, Lees, et al., 1968, 2Uncertainty assigned by TRC = 0.02 K; IPTS-48; TRC
Quantity Value Units Method Reference Comment
Tc548. ± 8.KAVGN/AAverage of 10 values; Individual data points
Quantity Value Units Method Reference Comment
Pc45. ± 5.barAVGN/AAverage of 6 values; Individual data points
Quantity Value Units Method Reference Comment
Vc0.274l/molN/AGude and Teja, 1995 
Quantity Value Units Method Reference Comment
ρc3.66 ± 0.02mol/lN/AGude and Teja, 1995 
ρc3.672mol/lN/AAmbrose and Townsend, 1963TRC
ρc3.63mol/lN/AKay and Donham, 1955TRC
Quantity Value Units Method Reference Comment
Δvap51. ± 1.kJ/molAVGN/AAverage of 10 out of 11 values; Individual data points

Enthalpy of vaporization

ΔvapH (kJ/mol) Temperature (K) Method Reference Comment
41.82381.1N/AMajer and Svoboda, 1985 
45.4365.EBSusial and Ortega, 1993Based on data from 350. to 400. K.; AC
49.5328.AStephenson and Malanowski, 1987Based on data from 313. to 411. K.; AC
46.0396.AStephenson and Malanowski, 1987Based on data from 381. to 524. K.; AC
55.0228.AStephenson and Malanowski, 1987Based on data from 202. to 243. K.; AC
44.2379.AStephenson and Malanowski, 1987Based on data from 369. to 389. K.; AC
42.6398.AStephenson and Malanowski, 1987Based on data from 383. to 416. K.; AC
41.1416.AStephenson and Malanowski, 1987Based on data from 401. to 493. K.; AC
36.2498.AStephenson and Malanowski, 1987Based on data from 483. to 548. K.; AC
46.2357.A,EBStephenson and Malanowski, 1987Based on data from 342. to 389. K. See also Ambrose, Counsell, et al., 1970.; AC
49.7 ± 0.1313.CMajer, Svoboda, et al., 1984AC
48.3 ± 0.1328.CMajer, Svoboda, et al., 1984AC
45.0 ± 0.1358.CMajer, Svoboda, et al., 1984AC
48.1335.N/ASachek, Peshchenko, et al., 1982Based on data from 320. to 382. K.; AC
52.6308.N/AWilhoit and Zwolinski, 1973Based on data from 293. to 388. K.; AC
46.2 ± 0.1347.CCounsell, Fenwick, et al., 1970AC
44.2 ± 0.1363.CCounsell, Fenwick, et al., 1970AC
41.9 ± 0.1381.CCounsell, Fenwick, et al., 1970AC
47.0348.N/ABrown, Fock, et al., 1969Based on data from 333. to 381. K. See also Boublik, Fried, et al., 1984.; AC
40.1438.N/AAmbrose and Townsend, 1963, 2Based on data from 423. to 548. K.; AC
45.2368.EBBiddiscombe, Collerson, et al., 1963Based on data from 353. to 388. K.; AC
50.71106.90VSkinner and Snelson, 1960ALS

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 381.
A (kJ/mol) 49.05
α -1.6587
β 1.1038
Tc (K) 547.7
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
422.64 to 547.714.400621260.453-92.588Ambrose and Townsend, 1963, 3Coefficents calculated by NIST from author's data.
353.36 to 388.774.431261236.991-101.528Biddiscombe, Collerson, et al., 1963, 2Coefficents calculated by NIST from author's data.

Enthalpy of fusion

ΔfusH (kJ/mol) Temperature (K) Reference Comment
6.322171.18Counsell, Lees, et al., 1968DH
6.32171.2Counsell, Lees, et al., 1968, 2AC

Entropy of fusion

ΔfusS (J/mol*K) Temperature (K) Reference Comment
36.93171.18Counsell, Lees, et al., 1968DH

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) = 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
100. MN/A
83. MButler, Ramchandani, et al., 1935

Gas phase ion energetics data

Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Henry's Law data, Ion clustering data, Mass spectrum (electron ionization), 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

Quantity Value Units Method Reference Comment
IE (evaluated)10.02 ± 0.02eVN/AN/AL
Quantity Value Units Method Reference Comment
Proton affinity (review)793.7kJ/molN/AHunter and Lias, 1998HL
Quantity Value Units Method Reference Comment
Gas basicity762.2kJ/molN/AHunter and Lias, 1998HL

Ionization energy determinations

IE (eV) Method Reference Comment
10.02 ± 0.05PIPECOShao, Baer, et al., 1988LL
10.11 ± 0.07EIBowen and Maccoll, 1984LBLHLM
10.12 ± 0.04EIHolmes, Fingas, et al., 1981LLK
10.09 ± 0.02PECocksey, Eland, et al., 1971LLK
10.47 ± 0.03PEPeel and Willett, 1975Vertical value; LLK

Appearance energy determinations

Ion AE (eV) Other Products MethodReferenceComment
CH5O+10.43 ± 0.03C3H5PIPECOShao, Baer, et al., 1988LL
CH5O+10.54 ± 0.05CH2CHCH2EIHolmes and Lossing, 1984LBLHLM
C3H6+11.00 ± 0.03CH3OHPIPECOShao, Baer, et al., 1988LL
C3H7+11.28 ± 0.05CH2OHPIPECOShao, Baer, et al., 1988LL
C4H8+10.33 ± 0.03H2OPIPECOShao, Baer, et al., 1988LL

De-protonation reactions

C4H9O- + Hydrogen cation = 1-Propanol, 2-methyl-

By formula: C4H9O- + H+ = C4H10O

Quantity Value Units Method Reference Comment
Δr1567. ± 8.4kJ/molCIDCHaas and Harrison, 1993gas phase; Both metastable and 50 eV collision energy.; B
Δr1568. ± 8.8kJ/molG+TSBartmess, Scott, et al., 1979gas phase; value altered from reference due to change in acidity scale; B
Quantity Value Units Method Reference Comment
Δr1539. ± 8.8kJ/molH-TSHaas and Harrison, 1993gas phase; Both metastable and 50 eV collision energy.; B
Δr1540. ± 8.4kJ/molIMREBartmess, Scott, et al., 1979gas phase; value altered from reference due to change in acidity scale; B

Ion clustering 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: Robert C. Dunbar

Note: Please consider using the reaction search for this species. This page allows searching of all reactions involving this species. Searches may be limited to ion clustering reactions. A general reaction search form is also available.

Clustering reactions

Lithium ion (1+) + 1-Propanol, 2-methyl- = (Lithium ion (1+) • 1-Propanol, 2-methyl-)

By formula: Li+ + C4H10O = (Li+ • C4H10O)

Quantity Value Units Method Reference Comment
Δr169. ± 7.9kJ/molCIDTRodgers and Armentrout, 2000 

Sodium ion (1+) + 1-Propanol, 2-methyl- = (Sodium ion (1+) • 1-Propanol, 2-methyl-)

By formula: Na+ + C4H10O = (Na+ • C4H10O)

Quantity Value Units Method Reference Comment
Δr105. ± 5.9kJ/molCIDTRodgers and Armentrout, 2000 
Δr105. ± 5.9kJ/molCIDTRodgers and Armentrout, 1999 

Mass spectrum (electron ionization)

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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: NIST Mass Spectrometry Data Center, William E. Wallace, director

Spectrum

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Mass spectrum
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Additional Data

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Due to licensing restrictions, this spectrum cannot be downloaded.

Owner NIST Mass Spectrometry Data Center
Collection (C) 2014 copyright by the U.S. Secretary of Commerce
on behalf of the United States of America. All rights reserved.
Origin NIST Mass Spectrometry Data Center, 1998.
NIST MS number 290809

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References

Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics data, Ion clustering data, Mass spectrum (electron ionization), Notes

Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.

Connett, 1975
Connett, J.E., Chemical equilibria 6. Measurement of equilibrium constants for the dehydrogenation of 2-methylpropan-1-ol by a vapour-flow technique, J. Chem. Thermodyn., 1975, 7, 1159-1162. [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]

Skinner and Snelson, 1960
Skinner, H.A.; Snelson, A., The heats of combustion of the four isomeric butyl alcohols, Trans. Faraday Soc., 1960, 56, 1776-1783. [all data]

Counsell J.F., 1968
Counsell J.F., Thermodynamic properties of organic oxygen compounds. Part XIX. Low-temperature heat capacity and entropy of propan-1-ol, 2-methylpropan-1-ol, and pentan-1-ol, J. Chem. Soc. A, 1968, 1819-1823. [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]

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]

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]

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]

Counsell, Lees, et al., 1968
Counsell, J.F.; Lees, E.B.; Martin, J.F., Thermodynamic properties of organic oxygen compounds. Part XIX. Low temperature heat capacity and entropy of propan-1-ol, 2-methyl-propan-1-ol, and pentan-1-ol, 1968, J. [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]

Piekarski and Somsen, 1988
Piekarski, H.; Somsen, G., Heat capacities and volumes of mixtures of N,N-dimethylformamide with isobutanol, sec-butanol and t-pentanol, J. Chem. Soc., Faraday Trans. 1, 1988, 84(2), 529-537. [all data]

Rybalkin, Emel'yanov, et al., 1978
Rybalkin, V.I.; Emel'yanov, V.M.; Stupak, P.M.; Litovchenko, N.P.; Z'ola, M.I., Study of the heat capacity of initial compounds and reaction products in the production of metal dialkyldithiophosphates, B.S.R. Inst. Neftepererab. Neftekhim. Prom. (Kiev), 1978, (16), 48-50. [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]

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]

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]

Zhdanov, 1941
Zhdanov, A.K., Specific heats of some liquids and azeotropic mixtures, Zhur. Obshch. Khim., 1941, 11, 471-482. [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]

Anonymous, 1958
Anonymous, X., Am. Pet. Inst. Res. Proj. 50, 1958, Unpublished, 1958. [all data]

Kanda, Otsubo, et al., 1950
Kanda, E.; Otsubo, A.; Haseda, T., Sci. Rep. Res. Inst., Tohoku Univ. Ser. A, 1950, 2, 9. [all data]

Wilhoit, Chao, et al., 1985
Wilhoit, R.C.; Chao, J.; Hall, K.R., Thermodynamic Properties of Key Organic Compounds in the Carbon Range C1 to C4. Part 1. Properties of Condensed Phases, J. Phys. Chem. Ref. Data, 1985, 14, 1. [all data]

Counsell, Lees, et al., 1968, 2
Counsell, J.F.; Lees, E.B.; Martin, J.F., Thermodynamic properties of organic oxygen compounds. Part XIX. Low-temperature heat capacity and entropy of propan-1-ol, 2-methylpropan-1-ol, and pentan-1-ol, J. Chem. Soc., A, 1968, 1819, https://doi.org/10.1039/j19680001819 . [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]

Ambrose and Townsend, 1963
Ambrose, D.; Townsend, R., Thermodynamic Properties of Organic Oxygen Compounds IX. The Critical Properties and Vapor Pressures Above Five Atmospheres of Six Aliphatic Alcohols, J. Chem. Soc., 1963, 54, 3614-25. [all data]

Kay and Donham, 1955
Kay, W.B.; Donham, W.E., Liquid-Vapor Equilibrium in the Isobutyl Alcohol-Butanol, Methanol- Butanol, and Diethyl Ether-Butanol Systems, Chem. Eng. Sci., 1955, 4, 1-16. [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]

Susial and Ortega, 1993
Susial, Pedro; Ortega, Juan, Isobaric vapor-liquid equilibria for methyl propanoate + isobutyl alcohol, J. Chem. Eng. Data, 1993, 38, 3, 434-436, https://doi.org/10.1021/je00011a028 . [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]

Majer, Svoboda, et al., 1984
Majer, V.; Svoboda, V.; Hynek, V., On the enthalpy of vaporization of isomeric butanols, J. Chem. Thermodyn., 1984, 16, 1059-1066. [all data]

Sachek, Peshchenko, et al., 1982
Sachek, A.I.; Peshchenko, A.D.; Markovnik, V.S.; Ral'ko, O.V.; Andreevskii, D.N.; Leont'eva, A.A., Termodin. Org. Soedin., 1982, 94. [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]

Brown, Fock, et al., 1969
Brown, I.; Fock, W.; Smith, F., The thermodynamic properties of solutions of normal and branched alcohols in benzene and n-hexane, The Journal of Chemical Thermodynamics, 1969, 1, 3, 273-291, https://doi.org/10.1016/0021-9614(69)90047-0 . [all data]

Boublik, Fried, et al., 1984
Boublik, T.; Fried, V.; Hala, E., The Vapour Pressures of Pure Substances: Selected Values of the Temperature Dependence of the Vapour Pressures of Some Pure Substances in the Normal and Low Pressure Region, 2nd ed., Elsevier, New York, 1984, 972. [all data]

Ambrose and Townsend, 1963, 2
Ambrose, D.; Townsend, R., 681. Thermodynamic properties of organic oxygen compounds. Part IX. The critical properties and vapour pressures, above five atmospheres, of six aliphatic alcohols, J. Chem. Soc., 1963, 3614, https://doi.org/10.1039/jr9630003614 . [all data]

Biddiscombe, Collerson, et al., 1963
Biddiscombe, D.P.; Collerson, R.R.; Handley, R.; Herington, E.F.G.; Martin, J.F.; Sprake, C.H.S., 364. Thermodynamic properties of organic oxygen compounds. Part VIII. Purification and vapour pressures of the propyl and butyl alcohols, J. Chem. Soc., 1963, 1954, https://doi.org/10.1039/jr9630001954 . [all data]

Ambrose and Townsend, 1963, 3
Ambrose, D.; Townsend, R., Thermodynamic Properties of Organic Oxygen Compounds. Part 9. The Critical Properties and Vapour Pressures, above Five Atmospheres, of Six Aliphatic Alcohols, J. Chem. Soc., 1963, 3614-3625, https://doi.org/10.1039/jr9630003614 . [all data]

Biddiscombe, Collerson, et al., 1963, 2
Biddiscombe, D.P.; Collerson, R.R.; Handley, R.; Herington, E.F.G.; Martin, J.F.; Sprake, C.H.S., Thermodynamic Properties of Organic Oxygen Compounds. Part 8. Purification and Vapor Pressures of the Propyl and Butyl Alcohols, J. Chem. Soc., 1963, 1954-1957, https://doi.org/10.1039/jr9630001954 . [all data]

Butler, Ramchandani, et al., 1935
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Notes

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