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2-Butanol

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Gas phase thermochemistry data

Go To: Top, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, IR Spectrum, 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 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
Deltafgas-293.1kJ/molN/AChao and Rossini, 1965Value computed using «DELTA»fHliquid° value of -342.7±0.6 kj/mol from Chao and Rossini, 1965 and «DELTA»vapH° value of 49.6 kj/mol from Skinner and Snelson, 1960.; DRB
Deltafgas-293. ± 1.5kJ/molCcbSkinner and Snelson, 1960ALS
Quantity Value Units Method Reference Comment
gas355.37J/mol*KN/AChao J., 1986p=1 bar. Other third-law value of entropy at 298.15 K is 357.2 J/mol*K [ Andon R.J.L., 1971]. The value of S(298.15 K)=358.5 J/mol*K was obtained from equilibrium studies [ Buckley E., 1965].; GT

Constant pressure heat capacity of gas

Cp,gas (J/mol*K) Temperature (K) Reference Comment
41.8750.Thermodynamics Research Center, 1997p=1 bar. Calculated entropy at 298.15 K is 4.1 J/mol*K higher than the third-law value. Authors [ Chao J., 1986] believe that this is greater than the expected experimental uncertainty and reflects the approximations made in the calculated value. However, it should be noted that other experimental values of S(298.15 K), 357.2 [ Andon R.J.L., 1971] and 358.5 J/mol*K [ Buckley E., 1965], are in better agreement with calculated value. Selected S(T) and Cp(T) values agree with other statistically calculated values [62BER/MCC] within 1 J/mol*K. Values calculated by [ Rodionov P.P., 1969] are up to 9 and 11 J/mol*K lower than selected ones fo Cp(T) and S(T) values, respectively. Please also see Chao J., 1986.; GT
59.06100.
74.17150.
86.94200.
105.90273.15
112.74 ± 0.17298.15
113.25300.
140.74400.
165.63500.
186.83600.
204.82700.
220.27800.
233.65900.
245.301000.
255.451100.
264.301200.
272.031300.
278.771400.
284.661500.
296.41750.
304.92000.
311.22250.
315.92500.
319.42750.
322.13000.

Constant pressure heat capacity of gas

Cp,gas (J/mol*K) Temperature (K) Reference Comment
131.71 ± 0.40365.15Stromsoe 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 0.67 J/mol*K. The accuracy of the experimental heat capacities [ Stromsoe E., 1970] is estimated as less than 0.3%. Please also see Berman N.S., 1962.; GT
137.87 ± 0.67380.95
136.52 ± 0.41383.15
139.10 ± 0.67386.25
140.85 ± 0.67393.75
141.46 ± 0.42401.15
143.50 ± 0.67405.15
143.74 ± 0.67406.15
146.32 ± 0.67417.25
146.23 ± 0.44419.15
150.96 ± 0.45437.15
151.79 ± 0.67440.75
155.64 ± 0.47455.15
158.81 ± 0.67470.85
169.31 ± 0.67515.95
179.65 ± 0.67560.35
184.89 ± 0.67582.85

Condensed phase thermochemistry data

Go To: Top, Gas phase thermochemistry data, Phase change data, Reaction thermochemistry data, IR Spectrum, 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 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
Deltafliquid-342.7 ± 0.59kJ/molCcbChao and Rossini, 1965see Rossini, 1934; ALS
Deltafliquid-342.6 ± 0.92kJ/molCcbSkinner and Snelson, 1960ALS
Quantity Value Units Method Reference Comment
Deltacliquid-2660.6 ± 0.54kJ/molCcbChao and Rossini, 1965see Rossini, 1934; Corresponding «DELTA»fliquid = -342.6 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS
Deltacliquid-2660.6 ± 0.92kJ/molCcbSkinner and Snelson, 1960Corresponding «DELTA»fliquid = -342.5 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS
Quantity Value Units Method Reference Comment
liquid213.1J/mol*KN/AAndon, Connett, et al., 1971DH
liquid214.7J/mol*KN/AAndon, Connett, et al., 1971DH

Constant pressure heat capacity of liquid

Cp,liquid (J/mol*K) Temperature (K) Reference Comment
197.1298.15N/ADH
198.03298.15Okano, Ogawa, et al., 1988DH
196.67298.15Piekarski and Somsen, 1988DH
199.2298.Conti, Gianni, et al., 1976DH
197.4298.15Andon, Connett, et al., 1971T = 11 to 350 K.; DH
196.8298.15Andon, Connett, et al., 1971T = 11 to 350 K.; DH
184.9281.7Parks, Thomas, et al., 1936T = 103 to 282 K. Glass at lower temperature. Unsmoothed experimental datum.; 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
DH - Eugene S. Domalski and Elizabeth D. Hearing

Quantity Value Units Method Reference Comment
Tboil372. ± 1.KAVGN/AAverage of 70 out of 72 values; Individual data points
Quantity Value Units Method Reference Comment
Tfus158.45KN/AAnonymous, 1968TRC
Quantity Value Units Method Reference Comment
Ttriple184.73KN/AWilhoit, Chao, et al., 1985Uncertainty assigned by TRC = 0.1 K; TRC
Ttriple184.70KN/AAndon, Connett, et al., 1971, 2Uncertainty assigned by TRC = 0.02 K; TRC
Quantity Value Units Method Reference Comment
Tc536. ± 1.KAVGN/AAverage of 8 values; Individual data points
Quantity Value Units Method Reference Comment
Pc42.0 ± 0.2barAVGN/AAverage of 6 values; Individual data points
Quantity Value Units Method Reference Comment
Vc0.269l/molN/AGude and Teja, 1995 
Quantity Value Units Method Reference Comment
rhoc3.72 ± 0.02mol/lN/AGude and Teja, 1995 
rhoc3.72mol/lN/ATeja, Lee, et al., 1989TRC
rhoc3.717mol/lN/AAmbrose and Townsend, 1963TRC
Quantity Value Units Method Reference Comment
Deltavap48. ± 5.kJ/molAVGN/AAverage of 9 values; Individual data points

Enthalpy of vaporization

DeltavapH (kJ/mol) Temperature (K) Method Reference Comment
40.75372.7N/AMajer and Svoboda, 1985 
48.8330.EBGierycz, Kosowski, et al., 2009Based on data from 315. - 371. K.; AC
46.2335.N/AMartínez, Lladosa, et al., 2009Based on data from 320. - 379. K.; AC
47.7321.N/ADejoz, Cruz Burguet, et al., 1995Based on data from 306. - 373. K.; AC
49.3318.AStephenson and Malanowski, 1987Based on data from 303. - 403. K.; AC
43.2370.AStephenson and Malanowski, 1987Based on data from 359. - 381. K.; AC
47.9387.AStephenson and Malanowski, 1987Based on data from 372. - 524. K.; AC
57.5225.AStephenson and Malanowski, 1987Based on data from 210. - 303. K.; AC
43.2369.AStephenson and Malanowski, 1987Based on data from 359. - 380. K.; AC
42.383.AStephenson and Malanowski, 1987Based on data from 368. - 404. K.; AC
39.6410.AStephenson and Malanowski, 1987Based on data from 395. - 485. K.; AC
35.491.AStephenson and Malanowski, 1987Based on data from 476. - 536. K.; AC
44.7355.EBStephenson and Malanowski, 1987Based on data from 340. - 379. K. See also Berman and McKetta, 1962 and Ambrose, Counsell, et al., 1970.; AC
47.8322.N/ASachek, Peshchenko, et al., 1982Based on data from 307. - 373. K.; AC
53.2308.N/ADi Cave, Chianese, et al., 1978Based on data from 293. - 380. K.; AC
44.1334.N/ABrazhnikov, Andreevskii, et al., 1975Based on data from 319. - 372. K.; AC
50.2295.N/ACabani, Conti, et al., 1975Based on data from 280. - 314. K.; AC
48.1313.N/AWilhoit and Zwolinski, 1973Based on data from 298. - 393. K.; AC
46.3338.N/ABrown, Fock, et al., 1969Based on data from 323. - 373. K. See also Boublik, Fried, et al., 1984.; AC
44.1360.EBBiddiscombe, Collerson, et al., 1963Based on data from 345. - 381. K.; AC
45.3 ± 0.1340.CBerman and McKetta, 1962AC
43.3 ± 0.1355.CBerman and McKetta, 1962AC
41.9 ± 0.1365.CBerman and McKetta, 1962AC
40.8 ± 0.1372.CBerman and McKetta, 1962AC

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. - 372.
A (kJ/mol) 52.6
alpha -1.462
beta 1.0701
Tc (K) 536.
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
422.11 - 535.94.198271094.254-111.603Ambrose and Townsend, 1963, 2Coefficents calculated by NIST from author's data.
345.54 - 380.304.329431158.672-104.683Biddiscombe, Collerson, et al., 1963, 2Coefficents calculated by NIST from author's data.

Enthalpy of fusion

DeltafusH (kJ/mol) Temperature (K) Reference Comment
6.000177.38Andon, Connett, et al., 1971DH
5.970184.70Andon, Connett, et al., 1971DH
5.97184.7Andon, Connett, et al., 1971, 3AC

Entropy of fusion

DeltafusS (J/mol*K) Temperature (K) Reference Comment
33.83177.38Andon, Connett, et al., 1971DH
32.32184.70Andon, Connett, et al., 1971DH

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:


Reaction thermochemistry data

Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, IR Spectrum, 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 compiled as indicated in comments:
B - John E. Bartmess
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
RCD - Robert C. Dunbar

Note: Please consider using the reaction search for this species. This page allows searching of all reactions involving this species. A general reaction search form is also available. Future versions of this site may rely on reaction search pages in place of the enumerated reaction displays seen below.

Individual Reactions

C4H9O- + Hydrogen cation = 2-Butanol

By formula: C4H9O- + H+ = C4H10O

Quantity Value Units Method Reference Comment
Deltar1565. ± 8.4kJ/molCIDCHaas and Harrison, 1993gas phase; Both metastable and 50 eV collision energy.; B
Deltar1566. ± 8.8kJ/molG+TSTaft, 1987gas phase; value altered from reference due to change in acidity scale; B
Deltar1565. ± 12.kJ/molG+TSBoand, Houriet, et al., 1983gas phase; value altered from reference due to change in acidity scale; B
Quantity Value Units Method Reference Comment
Deltar1538. ± 8.8kJ/molH-TSHaas and Harrison, 1993gas phase; Both metastable and 50 eV collision energy.; B
Deltar1538. ± 8.4kJ/molIMRETaft, 1987gas phase; value altered from reference due to change in acidity scale; B
Deltar1538. ± 11.kJ/molCIDCBoand, Houriet, et al., 1983gas phase; value altered from reference due to change in acidity scale; B

Hydrogen + 2-Butanone = 2-Butanol

By formula: H2 + C4H8O = C4H10O

Quantity Value Units Method Reference Comment
Deltar-54.18kJ/molEqkBuckley and Herington, 1965gas phase; ALS
Deltar-54.3 ± 0.4kJ/molChydDolliver, Gresham, et al., 1938gas phase; Reanalyzed by Cox and Pilcher, 1970, Original value = -55.2 ± 0.4 kJ/mol; At 355 °K; ALS

2-Butanol = Hydrogen + 2-Butanone

By formula: C4H10O = H2 + C4H8O

Quantity Value Units Method Reference Comment
Deltar54.22kJ/molEqkCubberley and Mueller, 1946gas phase; ALS
Deltar57.170kJ/molEqkKolb and Burwell, 1945gas phase; ALS

1-Propene, 2-methyl- + 2-Butanol = 2-(tert-butoxy)butane

By formula: C4H8 + C4H10O = C8H18O

Quantity Value Units Method Reference Comment
Deltar-37.7 ± 2.4kJ/molEqkSharonov, Mishentseva, et al., 1991liquid phase; ALS

Ketene + 2-Butanol = sec-Butyl acetate

By formula: C2H2O + C4H10O = C6H12O2

Quantity Value Units Method Reference Comment
Deltar-144.5kJ/molCmRice and Greenberg, 1934liquid phase; ALS

Sodium ion (1+) + 2-Butanol = (Sodium ion (1+) bullet 2-Butanol)

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

Quantity Value Units Method Reference Comment
Deltar117. ± 5.0kJ/molCIDTRodgers and Armentrout, 1999RCD

Lithium ion (1+) + 2-Butanol = (Lithium ion (1+) bullet 2-Butanol)

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

Quantity Value Units Method Reference Comment
Deltar174. ± 9.2kJ/molCIDTRodgers and Armentrout, 2000RCD

IR Spectrum

Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, Mass spectrum (electron ionization), References, Notes

Data compiled by: Coblentz Society, Inc.

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


Mass spectrum (electron ionization)

Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, IR Spectrum, 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: NIST Mass Spectrometry Data Center, William E. Wallace, director

Spectrum

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Additional Data

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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 R.A.FRIEDEL BUREAU OF MINES U.S.DEPT.OF INT.BRUCETON PA U.S.A.
NIST MS number 19165

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References

Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Reaction thermochemistry data, IR Spectrum, 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.

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]

Chao J., 1986
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]

Andon R.J.L., 1971
Andon R.J.L., Thermodynamic properties of organic oxygen compounds. Part XXVII. (+/-)-Butan-2-ol and (+)-butan-2-ol, J. Chem. Soc. A, 1971, 661-664. [all data]

Buckley E., 1965
Buckley E., Equilibria in some secondary alcohol + hydrogen + ketone systems, Trans. Faraday Soc., 1965, 61, 1618-1625. [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]

Rodionov P.P., 1969
Rodionov P.P., Thermodynamic functions of 2-butanol (d,l), Izv. Vyssh. Ucheb. Zaved., Khim. Khim. Tekhnol., 1969, 12, 1214-1218. [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]

Berman N.S., 1962
Berman N.S., Thermodynamic properties of 2-butanol, J. Phys. Chem., 1962, 66, 1444-1448. [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]

Andon, Connett, et al., 1971
Andon, R.J.; Connett, J.E.; Counsell, J.F.; Lees, E.B.; Martin, J.F., Thermodynamic properties of organic oxygen compounds. Part XXVII. (±)-Butan-2-ol and (+)-Butan-2-ol, 1971, 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]

Conti, Gianni, et al., 1976
Conti, G.; Gianni, P.; Matteoli, E.; Mengheri, M., Capacita termiche molari di alcuni composti organici mono- e bifunzionali nel liquido puro e in soluzione acquosa a 25C, Chim. Ind. (Milan), 1976, 58, 225. [all data]

Parks, Thomas, et al., 1936
Parks, G.S.; Thomas, S.B.; Light, D.W., XII. Some new heat capacity data for organic glasses. The entropy and free energy of DL-lactic acid, J. Chem. Phys., 1936, 4, 64-69. [all data]

Anonymous, 1968
Anonymous, X., Chemicals and Plastics Physical Properties, 1968, Union Carbide Corp., product bulletin, 1968. [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]

Andon, Connett, et al., 1971, 2
Andon, R.J.L.; Connett, J.E.; Counsell, J.F.; Lees, E.B.; Martin, J.F., Thermodynamic properties of organic oxygen compounds: xxvii racemate of - butan-2-ol and (+)-butan-2-ol, J. Chem. Soc. A, 1971, 1971, 661-4. [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]

Teja, Lee, et al., 1989
Teja, A.S.; Lee, R.J.; Rosenthal, D.J.; Anselme, M.J., Correlation of the Critical Properties of Alkanes and Alkanols in 5th IUPAC Conference on Alkanes and AlkanolsGradisca, 1989. [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]

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]

Gierycz, Kosowski, et al., 2009
Gierycz, Pawel; Kosowski, Andrzej; Swietlik, Ryszard, Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols, J. Chem. Eng. Data, 2009, 54, 11, 2996-3001, https://doi.org/10.1021/je900050z . [all data]

Martínez, Lladosa, et al., 2009
Martínez, Nelson F.; Lladosa, Estela; Burguet, MªCruz; Montón, Juan B.; Yazimon, Marlen, Isobaric vapour--liquid equilibria for the binary systems 4-methyl-2-pentanone+1-butanol and+2-butanol at 20 and 101.3kPa, Fluid Phase Equilibria, 2009, 277, 1, 49-54, https://doi.org/10.1016/j.fluid.2008.11.012 . [all data]

Dejoz, Cruz Burguet, et al., 1995
Dejoz, Ana; Cruz Burguet, M.; Munoz, Rosa; Sanchotello, Margarita, Isobaric Vapor-Liquid Equilibria of Tetrachloroethylene with 1-Butanol and 2-Butanol at 6 and 20 kPa, J. Chem. Eng. Data, 1995, 40, 1, 290-292, https://doi.org/10.1021/je00017a064 . [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]

Berman and McKetta, 1962
Berman, Neil S.; McKetta, John J., THE THERMODYNAMIC PROPERTIES OF 2-BUTANOL, J. Phys. Chem., 1962, 66, 8, 1444-1448, https://doi.org/10.1021/j100814a016 . [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]

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]

Di Cave, Chianese, et al., 1978
Di Cave, Sergio; Chianese, Angelo; Prantera, Antonio, Vapor-liquid equilibrium of the system methylethylketone-sec-butyl alcohol, J. Chem. Eng. Data, 1978, 23, 4, 279-281, https://doi.org/10.1021/je60079a013 . [all data]

Brazhnikov, Andreevskii, et al., 1975
Brazhnikov, M.M.; Andreevskii, D.N.; Sachek, A.I.; Peshchenko, A.D., Zh. Prikl. Khim. (Leningrad), 1975, 48, 10, 2181. [all data]

Cabani, Conti, et al., 1975
Cabani, Sergio; Conti, G.; Mollica, V.; Lepori, L., Thermodynamic study of dilute aqueous solutions of organic compounds. Part 4.---Cyclic and straight chain secondary alcohols, J. Chem. Soc., Faraday Trans. 1, 1975, 71, 0, 1943, https://doi.org/10.1039/f19757101943 . [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]

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]

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, 2
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]

Andon, Connett, et al., 1971, 3
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Notes

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