1-Butanol

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Phase change data

Go To: Top, Reaction thermochemistry 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
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
Tboil390.6 ± 0.8KAVGN/AAverage of 137 out of 146 values; Individual data points
Quantity Value Units Method Reference Comment
Tfus188. ± 9.KAVGN/AAverage of 6 values; Individual data points
Quantity Value Units Method Reference Comment
Ttriple184.54KN/AWilhoit, Chao, et al., 1985Uncertainty assigned by TRC = 0.02 K; TRC
Ttriple184.51KN/ACounsell, Hales, et al., 1965Uncertainty assigned by TRC = 0.05 K; TRC
Ttriple183.9KN/AParks, 1925Uncertainty assigned by TRC = 0.2 K; TRC
Quantity Value Units Method Reference Comment
Tc562. ± 2.KAVGN/AAverage of 21 values; Individual data points
Quantity Value Units Method Reference Comment
Pc45. ± 4.barAVGN/AAverage of 10 values; Individual data points
Quantity Value Units Method Reference Comment
Vc0.274l/molN/AGude and Teja, 1995 
Quantity Value Units Method Reference Comment
ρc3.65 ± 0.06mol/lAVGN/AAverage of 7 values; Individual data points
Quantity Value Units Method Reference Comment
Δvap52. ± 3.kJ/molAVGN/AAverage of 15 out of 16 values; Individual data points

Enthalpy of vaporization

ΔvapH (kJ/mol) Temperature (K) Method Reference Comment
43.29390.9N/AMajer and Svoboda, 1985 
46.0372.EBMuñoz and Krähenbühl, 2001Based on data from 357. to 389. K.; AC
38.2423.N/AWormald and Fennell, 2000AC
29.6473.N/AWormald and Fennell, 2000AC
20.8523.N/AWormald and Fennell, 2000AC
49.9330.N/ADejoz, Cruz Burguet, et al., 1995Based on data from 315. to 390. K.; AC
45.3379.N/ASusial and Ortega, 1993Based on data from 364. to 403. K.; AC
45.3387.AStephenson and Malanowski, 1987Based on data from 376. to 399. K.; AC
50.1338.AStephenson and Malanowski, 1987Based on data from 323. to 413. K.; AC
41.9428.AStephenson and Malanowski, 1987Based on data from 413. to 550. K.; AC
51.6236.AStephenson and Malanowski, 1987Based on data from 209. to 251. K.; AC
45.4386.AStephenson and Malanowski, 1987Based on data from 376. to 397. K.; AC
43.8406.AStephenson and Malanowski, 1987Based on data from 391. to 429. K.; AC
41.9430.AStephenson and Malanowski, 1987Based on data from 415. to 501. K.; AC
37.4512.AStephenson and Malanowski, 1987Based on data from 497. to 563. K.; AC
47.2366.EBStephenson and Malanowski, 1987Based on data from 351. to 397. K. See also Ambrose, Counsell, et al., 1970.; AC
49.0344.N/ASachek, Peshchenko, et al., 1982Based on data from 329. to 391. K.; AC
49.5 ± 0.1333.CSvoboda, Veselý, et al., 1973AC
48.6 ± 0.1343.CSvoboda, Veselý, et al., 1973AC
47.5 ± 0.1353.CSvoboda, Veselý, et al., 1973AC
46.4 ± 0.1363.CSvoboda, Veselý, et al., 1973AC
55.0303.N/AWilhoit and Zwolinski, 1973Based on data from 288. to 404. K.; AC
53.0310.DTAKemme and Kreps, 1969Based on data from 295. to 391. K.; AC
47.2 ± 0.1356.CCounsell, Hales, et al., 1965AC
45.4 ± 0.1381.CCounsell, Hales, et al., 1965AC
43.1 ± 0.1391.CCounsell, Hales, et al., 1965AC
42.1434.N/AAmbrose and Townsend, 1963Based on data from 419. to 563. K.; AC
46.6377.EBBiddiscombe, Collerson, et al., 1963Based on data from 362. to 398. K.; AC
48.3352.N/ABrown and Smith, 1959Based on data from 337. to 390. K. See also Boublik, Fried, et al., 1984.; AC
48.3352.N/AKahlbaum, 1898Based on data from 314. to 390. K. See also Boublik, Fried, et al., 1984.; 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 410.
A (kJ/mol) 62.53
α -0.6584
β 0.696
Tc (K) 562.9
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
295.8 to 391.04.546071351.555-93.34Kemme and Kreps, 1969 
391. to 479.4.390311254.502-105.246Hessel and Geiseler, 1965Coefficents calculated by NIST from author's data.
419.34 to 562.984.429211305.001-94.676Ambrose and Townsend, 1963, 2Coefficents calculated by NIST from author's data.
362.36 to 398.844.503931313.878-98.789Biddiscombe, Collerson, et al., 1963, 2Coefficents calculated by NIST from author's data.

Enthalpy of fusion

ΔfusH (kJ/mol) Temperature (K) Reference Comment
9.372184.5Counsell, Hales, et al., 1965, 2DH
9.28183.9Acree, 1991AC
9.280183.9Parks, 1925, 2DH

Entropy of fusion

ΔfusS (J/mol*K) Temperature (K) Reference Comment
50.79184.5Counsell, Hales, et al., 1965, 2DH
50.46183.9Parks, 1925, 2DH

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, 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 as indicated in comments:
B - John E. Bartmess
M - Michael M. Meot-Ner (Mautner) and Sharon G. Lias
RCD - Robert C. Dunbar
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein

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 = 1-Butanol

By formula: C4H9O- + H+ = C4H10O

Quantity Value Units Method Reference Comment
Δr1570. ± 8.4kJ/molCIDCHaas and Harrison, 1993gas phase; Both metastable and 50 eV collision energy.; B
Δr1571. ± 8.8kJ/molG+TSBartmess, Scott, et al., 1979gas phase; value altered from reference due to change in acidity scale; B
Δr1569. ± 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
Δr1543. ± 8.8kJ/molH-TSHaas and Harrison, 1993gas phase; Both metastable and 50 eV collision energy.; B
Δr1543. ± 8.4kJ/molIMREBartmess, Scott, et al., 1979gas phase; value altered from reference due to change in acidity scale; B
Δr1541. ± 12.kJ/molCIDCBoand, Houriet, et al., 1983gas phase; value altered from reference due to change in acidity scale; B

C4H11O+ + 1-Butanol = (C4H11O+ • 1-Butanol)

By formula: C4H11O+ + C4H10O = (C4H11O+ • C4H10O)

Bond type: Hydrogen bonds of the type OH-O between organics

Quantity Value Units Method Reference Comment
Δr132.kJ/molICRLarson and McMahon, 1982gas phase; switching reaction((CH3)2OH+)(CH3)2O, Entropy change calculated or estimated; Grimsrud and Kebarle, 1973, Lias, Liebman, et al., 1984; M
Quantity Value Units Method Reference Comment
Δr129.J/mol*KN/ALarson and McMahon, 1982gas phase; switching reaction((CH3)2OH+)(CH3)2O, Entropy change calculated or estimated; Grimsrud and Kebarle, 1973, Lias, Liebman, et al., 1984; M
Quantity Value Units Method Reference Comment
Δr93.3kJ/molICRLarson and McMahon, 1982gas phase; switching reaction((CH3)2OH+)(CH3)2O, Entropy change calculated or estimated; Grimsrud and Kebarle, 1973, Lias, Liebman, et al., 1984; M

C3H9Si+ + 1-Butanol = (C3H9Si+ • 1-Butanol)

By formula: C3H9Si+ + C4H10O = (C3H9Si+ • C4H10O)

Quantity Value Units Method Reference Comment
Δr185.kJ/molPHPMSWojtyniak and Stone, 1986gas phase; switching reaction,Thermochemical ladder((CH3)3Si+)H2O, Entropy change calculated or estimated; M
Quantity Value Units Method Reference Comment
Δr130.J/mol*KN/AWojtyniak and Stone, 1986gas phase; switching reaction,Thermochemical ladder((CH3)3Si+)H2O, Entropy change calculated or estimated; M

Free energy of reaction

ΔrG° (kJ/mol) T (K) Method Reference Comment
124.468.PHPMSWojtyniak and Stone, 1986gas phase; switching reaction,Thermochemical ladder((CH3)3Si+)H2O, Entropy change calculated or estimated; M

C3H9Sn+ + 1-Butanol = (C3H9Sn+ • 1-Butanol)

By formula: C3H9Sn+ + C4H10O = (C3H9Sn+ • C4H10O)

Quantity Value Units Method Reference Comment
Δr153.kJ/molPHPMSStone and Splinter, 1984gas phase; switching reaction((CH3)3Sn+)CH3OH, Entropy change calculated or estimated; M
Quantity Value Units Method Reference Comment
Δr136.J/mol*KN/AStone and Splinter, 1984gas phase; switching reaction((CH3)3Sn+)CH3OH, Entropy change calculated or estimated; M

Free energy of reaction

ΔrG° (kJ/mol) T (K) Method Reference Comment
81.6525.PHPMSStone and Splinter, 1984gas phase; switching reaction((CH3)3Sn+)CH3OH, Entropy change calculated or estimated; M

CH6N+ + 1-Butanol = (CH6N+ • 1-Butanol)

By formula: CH6N+ + C4H10O = (CH6N+ • C4H10O)

Bond type: Hydrogen bonds of the type NH+-O between organics

Quantity Value Units Method Reference Comment
Δr98.3kJ/molPHPMSMeot-Ner, 1984gas phase; Entropy change calculated or estimated; M
Quantity Value Units Method Reference Comment
Δr110.J/mol*KN/AMeot-Ner, 1984gas phase; Entropy change calculated or estimated; M

Free energy of reaction

ΔrG° (kJ/mol) T (K) Method Reference Comment
44.4495.PHPMSMeot-Ner, 1984gas phase; Entropy change calculated or estimated; M

Fluorine anion + 1-Butanol = (Fluorine anion • 1-Butanol)

By formula: F- + C4H10O = (F- • C4H10O)

Quantity Value Units Method Reference Comment
Δr135. ± 8.4kJ/molIMRELarson and McMahon, 1983gas phase; B,M
Quantity Value Units Method Reference Comment
Δr108.J/mol*KN/ALarson and McMahon, 1983gas phase; switching reaction(F-)H2O, Entropy change calculated or estimated; Arshadi, Yamdagni, et al., 1970; M
Quantity Value Units Method Reference Comment
Δr103. ± 8.4kJ/molIMRELarson and McMahon, 1983gas phase; B,M

Chlorine anion + 1-Butanol = (Chlorine anion • 1-Butanol)

By formula: Cl- + C4H10O = (Cl- • C4H10O)

Quantity Value Units Method Reference Comment
Δr73.6 ± 8.4kJ/molIMRELarson and McMahon, 1984gas phase; B,M
Quantity Value Units Method Reference Comment
Δr97.1J/mol*KN/ALarson and McMahon, 1984gas phase; switching reaction(Cl-)CH3OH, Entropy change calculated or estimated; Larson and McMahon, 1984, 2; M
Quantity Value Units Method Reference Comment
Δr44.8 ± 8.4kJ/molIMRELarson and McMahon, 1984gas phase; B,M

Sodium ion (1+) + 1-Butanol = (Sodium ion (1+) • 1-Butanol)

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

Quantity Value Units Method Reference Comment
Δr109. ± 5.0kJ/molCIDTRodgers and Armentrout, 1999RCD

Free energy of reaction

ΔrG° (kJ/mol) T (K) Method Reference Comment
82.4298.IMREMcMahon and Ohanessian, 2000Anchor alanine=39.89; RCD

Butanal + Hydrogen = 1-Butanol

By formula: C4H8O + H2 = C4H10O

Quantity Value Units Method Reference Comment
Δr-81.88 ± 0.75kJ/molCmWiberg, Crocker, et al., 1991liquid phase; ALS
Δr-70.5 ± 1.3kJ/molChydBuckley and Cox, 1967gas phase; ALS

thiophenoxide anion + 1-Butanol = (thiophenoxide anion • 1-Butanol)

By formula: C6H5S- + C4H10O = (C6H5S- • C4H10O)

Quantity Value Units Method Reference Comment
Δr61.1kJ/molPHPMSSieck and Meot-ner, 1989gas phase; M
Quantity Value Units Method Reference Comment
Δr105.J/mol*KPHPMSSieck and Meot-ner, 1989gas phase; M

Benzene, isocyanato- + 1-Butanol = Carbamic acid, phenyl-, butyl ester

By formula: C7H5NO + C4H10O = C11H15NO2

Quantity Value Units Method Reference Comment
Δr-83.9 ± 4.4kJ/molCmPannone and Macosko, 1987liquid phase; ALS
Δr-105. ± 1.kJ/molCmLovering and Laidler, 1962solid phase; ALS

Fluorine anion + 1-Butanol = C4H9D10FO-

By formula: F- + C4H10O = C4H9D10FO-

Quantity Value Units Method Reference Comment
Δr101. ± 8.4kJ/molIMREWilkinson, Szulejko, et al., 1992gas phase; Reported relative to ROH..F-, 0.5 kcal/mol weaker.; B

Magnesium ion (1+) + 1-Butanol = (Magnesium ion (1+) • 1-Butanol)

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

Quantity Value Units Method Reference Comment
Δr270. ± 20.kJ/molICROperti, Tews, et al., 1988gas phase; switching reaction,Thermochemical ladder(Mg+)CH3OH; M

1-Butanol + Chloridosulfuric acid = Butyl sulfuric acid + Hydrogen chloride

By formula: C4H10O + ClHO3S = C4H10O4S + HCl

Quantity Value Units Method Reference Comment
Δr58. ± 1.kJ/molCmMarkitanova, Barsukov, et al., 1981liquid phase; solvent: Dichloromethane; Sulfation; ALS

1-Butanol + 2-Propenoic acid = 2-Propenoic acid, butyl ester + Water

By formula: C4H10O + C3H4O2 = C7H12O2 + H2O

Quantity Value Units Method Reference Comment
Δr16.kJ/molEqkSelyakova, Vytnov, et al., 1976liquid phase; Heat of esterification 60-180 C; ALS

Acetic acid, butyl ester + Water = Acetic acid + 1-Butanol

By formula: C6H12O2 + H2O = C2H4O2 + C4H10O

Quantity Value Units Method Reference Comment
Δr3.3 ± 0.2kJ/molCmWadso, 1958liquid phase; Heat of hydrolysis; ALS

Maleic anhydride + 1-Butanol = 2-Butenedioic acid (Z)-, monobutyl ester

By formula: C4H2O3 + C4H10O = C8H12O4

Quantity Value Units Method Reference Comment
Δr-39.kJ/molKinMerca, Poraicu, et al., 1978solid phase; solvent: n-Butanol; DTA; ALS

1-Propene, 2-methyl- + 1-Butanol = 1-Tert-butoxybutane

By formula: C4H8 + C4H10O = C8H18O

Quantity Value Units Method Reference Comment
Δr-34.8 ± 2.7kJ/molEqkSharonov, Mishentseva, et al., 1991liquid phase; ALS

Ketene + 1-Butanol = Acetic acid, butyl ester

By formula: C2H2O + C4H10O = C6H12O2

Quantity Value Units Method Reference Comment
Δr-146.9kJ/molCmRice and Greenberg, 1934liquid phase; ALS

Lithium ion (1+) + 1-Butanol = (Lithium ion (1+) • 1-Butanol)

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

Quantity Value Units Method Reference Comment
Δr178. ± 7.9kJ/molCIDTRodgers and Armentrout, 2000RCD

Gas phase ion energetics data

Go To: Top, Phase change data, Reaction 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 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

Quantity Value Units Method Reference Comment
IE (evaluated)9.99 ± 0.05eVN/AN/AL
Quantity Value Units Method Reference Comment
Proton affinity (review)789.2kJ/molN/AHunter and Lias, 1998HL
Quantity Value Units Method Reference Comment
Gas basicity758.9kJ/molN/AHunter and Lias, 1998HL

Ionization energy determinations

IE (eV) Method Reference Comment
10.10 ± 0.05EIHolmes and Lossing, 1991LL
9.99 ± 0.05PIPECOShao, Baer, et al., 1988LL
10.64 ± 0.07EIBowen and Maccoll, 1984LBLHLM
10.09 ± 0.02PECocksey, Eland, et al., 1971LLK
10.37PEBaker, Betteridge, et al., 1971LLK
10.37PEBaker, Betteridge, et al., 1971LLK
10.04PIWatanabe, Nakayama, et al., 1962RDSH
10.43PEBenoit and Harrison, 1977Vertical value; LLK
10.44 ± 0.03PEPeel and Willett, 1975Vertical value; LLK
10.37PEKatsumata, Iwai, et al., 1973Vertical value; LLK

Appearance energy determinations

Ion AE (eV) Other Products MethodReferenceComment
CH3O+11.36 ± 0.06n-C3H7EISelim and Helal, 1981LLK
CH3O+11.46?EILambdin, Tuffly, et al., 1959RDSH
C2H2O+11.23?EILambdin, Tuffly, et al., 1959RDSH
C4H8+10.18 ± 0.05H2OPIPECOShao, Baer, et al., 1988LL
C4H8+10.20 ± 0.10H2OEIBowen and Maccoll, 1984LBLHLM

De-protonation reactions

C4H9O- + Hydrogen cation = 1-Butanol

By formula: C4H9O- + H+ = C4H10O

Quantity Value Units Method Reference Comment
Δr1570. ± 8.4kJ/molCIDCHaas and Harrison, 1993gas phase; Both metastable and 50 eV collision energy.; B
Δr1571. ± 8.8kJ/molG+TSBartmess, Scott, et al., 1979gas phase; value altered from reference due to change in acidity scale; B
Δr1569. ± 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
Δr1543. ± 8.8kJ/molH-TSHaas and Harrison, 1993gas phase; Both metastable and 50 eV collision energy.; B
Δr1543. ± 8.4kJ/molIMREBartmess, Scott, et al., 1979gas phase; value altered from reference due to change in acidity scale; B
Δr1541. ± 12.kJ/molCIDCBoand, Houriet, et al., 1983gas phase; value altered from reference due to change in acidity scale; B

References

Go To: Top, Phase change data, Reaction thermochemistry 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.

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, Hales, et al., 1965
Counsell, J.F.; Hales, J.L.; Martin, J.F., Thermodynamic properties of organic oxygen compounds. Part 16.?Butyl alcohol, Trans. Faraday Soc., 1965, 61, 1869, https://doi.org/10.1039/tf9656101869 . [all data]

Parks, 1925
Parks, G.S., Thermal data on organic compounds: I the heat capacities and free energies of methyl, ethyl and n-butyl alcohol, J. Am. Chem. Soc., 1925, 47, 338-45. [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]

Muñoz and Krähenbühl, 2001
Muñoz, Laura A.L.; Krähenbühl, M. Alvina, Isobaric Vapor Liquid Equilibrium (VLE) Data of the Systems n -Butanol + Butyric Acid and n -Butanol + Acetic Acid, J. Chem. Eng. Data, 2001, 46, 1, 120-124, https://doi.org/10.1021/je000033u . [all data]

Wormald and Fennell, 2000
Wormald, C.J.; Fennell, D.P., Organometallics, 2000, 21, 3, 767-779, https://doi.org/10.1023/A:1006648903706 . [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]

Susial and Ortega, 1993
Susial, Pedro; Ortega, Juan, Isobaric vapor-liquid equilibria in the system methyl propanoate + n-butyl alcohol, J. Chem. Eng. Data, 1993, 38, 4, 647-649, https://doi.org/10.1021/je00012a044 . [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]

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]

Svoboda, Veselý, et al., 1973
Svoboda, V.; Veselý, F.; Holub, R.; Pick, J., Enthalpy data of liquids. II. The dependence of heats of vaporization of methanol, propanol, butanol, cyclohexane, cyclohexene, and benzene on temperature, Collect. Czech. Chem. Commun., 1973, 38, 12, 3539-3543, https://doi.org/10.1135/cccc19733539 . [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]

Kemme and Kreps, 1969
Kemme, Herbert R.; Kreps, Saul I., Vapor pressure of primary n-alkyl chlorides and alcohols, J. Chem. Eng. Data, 1969, 14, 1, 98-102, https://doi.org/10.1021/je60040a011 . [all data]

Ambrose and Townsend, 1963
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]

Brown and Smith, 1959
Brown, I.; Smith, F., Liquid-Vapour Equilibria. IX. The Systems n-Propanol + Benzene and n-Butanol + Benzene at 45°C, Aust. J. Chem., 1959, 12, 3, 407-621, https://doi.org/10.1071/CH9590407 . [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]

Kahlbaum, 1898
Kahlbaum, G.W.A., Z. Phys. Chem., Stoechiom. Verwandtschaftsl., 1898, 26, 577. [all data]

Hessel and Geiseler, 1965
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Notes

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