1-Butanol

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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:
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
Δfgas-66. ± 1.kcal/molAVGN/AAverage of 13 values; Individual data points
Quantity Value Units Method Reference Comment
gas86.515cal/mol*KN/AChao J., 1986Other values of S(298.15 K) based on low-temperature thermal measurements are (in J/mol*K): 363.17 [65COU/HAL], 362.33 [ Chermin H.A.G., 1961], and 361.9 [ Buckley E., 1967].; GT

Constant pressure heat capacity of gas

Cp,gas (cal/mol*K) Temperature (K) Reference Comment
10.1750.Thermodynamics Research Center, 1997p=1 bar. Recommended S(T) and Cp(T) values agree with those calculated by [ Chermin H.A.G., 1961] within 1.5 J/mol*K. S(T) values calculated by [ Dyatkina M.E., 1954] are different from values given here by 12-30 J/mol*K. Please also see Chao J., 1986.; GT
13.94100.
16.75150.
19.43200.
24.063273.15
25.820 ± 0.060298.15
25.951300.
33.021400.
39.297500.
44.546600.
48.956700.
52.715800.
55.963900.
58.7791000.
61.2281100.
63.3601200.
65.2151300.
66.8331400.
68.2461500.
71.061750.
73.092000.
74.622250.
75.742500.
76.602750.
77.253000.

Constant pressure heat capacity of gas

Cp,gas (cal/mol*K) Temperature (K) Reference Comment
33.68 ± 0.19395.25Stromsoe 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 0.79 J/mol*K. The accuracy of the experimental heat capacities [ Stromsoe E., 1970] is estimated as less than 0.3%.; GT
32.954398.15
34.18 ± 0.19404.15
34.46 ± 0.19409.15
33.953413.15
35.03 ± 0.19419.55
35.67 ± 0.19431.05
35.234433.15
36.23 ± 0.19441.15
36.487453.15
37.26 ± 0.19459.55
38.85 ± 0.19488.25
40.62 ± 0.19520.05
42.06 ± 0.19545.95
43.31 ± 0.19568.45
45.25 ± 0.19603.35

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-79. ± 1.kcal/molAVGN/AAverage of 7 values; Individual data points
Quantity Value Units Method Reference Comment
Δcliquid-638. ± 5.kcal/molAVGN/AAverage of 10 values; Individual data points
Quantity Value Units Method Reference Comment
liquid53.951cal/mol*KN/ACounsell, Hales, et al., 1965DH
liquid54.49cal/mol*KN/AParks, Kelley, et al., 1929Extrapolation below 90 K, 46.02 J/mol*K. Revision of previous data.; DH
liquid60.21cal/mol*KN/AParks, 1925Extrapolation below 90 K, 73.81 J/mol*K.; DH

Constant pressure heat capacity of liquid

Cp,liquid (cal/mol*K) Temperature (K) Reference Comment
42.271298.15Andreoli-Ball, Patterson, et al., 1988DH
42.225298.15Gates, Wood, et al., 1986T = 298.15 to 368.15 K.; DH
42.47298.Korolev, Kukharenko, et al., 1986DH
45.94321.05Naziev, Bashirov, et al., 1986T = 321.05, 349.20, 373.35 K. p = 0.1 MPa. Unsmoothed experimental datum given as 2.5934 kJ/kg*K.; DH
42.347298.15Ogawa and Murakami, 1986DH
42.058298.15Roux-Dexgranges, Grolier, et al., 1986DH
42.230298.15Tanaka, Toyama, et al., 1986DH
42.323298.15Zegers and Somsen, 1984DH
41.66293.15Arutyunyan, Bagdasaryan, et al., 1981T = 293 to 373 K. p = 0.1 MPa. Unsmoothed experimental datum given as 2.351 kJ/kg*K. Cp given from 293.15 to 533.15 for pressure range 10 to 60 MPa.; DH
43.40303.5Griigo'ev, Yanin, et al., 1979T = 303 to 462 K. p = 0.98 bar.; DH
42.90301.2Paz Andrade, Paz, et al., 1970T = 28, 40°C.; DH
42.311298.15Counsell, Hales, et al., 1965T = 11 to 323 K.; DH
45.20323.Swietoslawski and Zielenkiewicz, 1960Mean value 21 to 78°C.; DH
51.51302.6Phillip, 1939DH
43.81298.Trew and Watkins, 1933DH
41.90294.0Parks, 1925T = 90 to 294 K. Value is unsmoothed experimental datum.; DH
43.09303.Willams and Daniels, 1924T = 303 to 343 K. Equation only.; DH
41.71298.von Reis, 1881T = 290 to 390 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
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., 1965, 2Uncertainty assigned by TRC = 0.05 K; TRC
Ttriple183.9KN/AParks, 1925, 2Uncertainty 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.atmAVGN/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
Δvap12.4 ± 0.6kcal/molAVGN/AAverage of 15 out of 16 values; Individual data points

Enthalpy of vaporization

ΔvapH (kcal/mol) Temperature (K) Method Reference Comment
10.35390.9N/AMajer and Svoboda, 1985 
11.0372.EBMuñoz and Krähenbühl, 2001Based on data from 357. to 389. K.; AC
9.13423.N/AWormald and Fennell, 2000AC
7.07473.N/AWormald and Fennell, 2000AC
4.97523.N/AWormald and Fennell, 2000AC
11.9330.N/ADejoz, Cruz Burguet, et al., 1995Based on data from 315. to 390. K.; AC
10.8379.N/ASusial and Ortega, 1993Based on data from 364. to 403. K.; AC
10.8387.AStephenson and Malanowski, 1987Based on data from 376. to 399. K.; AC
12.0338.AStephenson and Malanowski, 1987Based on data from 323. to 413. K.; AC
10.0428.AStephenson and Malanowski, 1987Based on data from 413. to 550. K.; AC
12.3236.AStephenson and Malanowski, 1987Based on data from 209. to 251. K.; AC
10.9386.AStephenson and Malanowski, 1987Based on data from 376. to 397. K.; AC
10.5406.AStephenson and Malanowski, 1987Based on data from 391. to 429. K.; AC
10.0430.AStephenson and Malanowski, 1987Based on data from 415. to 501. K.; AC
8.94512.AStephenson and Malanowski, 1987Based on data from 497. to 563. K.; AC
11.3366.EBStephenson and Malanowski, 1987Based on data from 351. to 397. K. See also Ambrose, Counsell, et al., 1970.; AC
11.7344.N/ASachek, Peshchenko, et al., 1982Based on data from 329. to 391. K.; AC
11.8 ± 0.02333.CSvoboda, Veselý, et al., 1973AC
11.6 ± 0.02343.CSvoboda, Veselý, et al., 1973AC
11.4 ± 0.02353.CSvoboda, Veselý, et al., 1973AC
11.1 ± 0.02363.CSvoboda, Veselý, et al., 1973AC
13.1303.N/AWilhoit and Zwolinski, 1973Based on data from 288. to 404. K.; AC
12.7310.DTAKemme and Kreps, 1969Based on data from 295. to 391. K.; AC
11.3 ± 0.02356.CCounsell, Hales, et al., 1965, 2AC
10.9 ± 0.02381.CCounsell, Hales, et al., 1965, 2AC
10.3 ± 0.02391.CCounsell, Hales, et al., 1965, 2AC
10.1434.N/AAmbrose and Townsend, 1963Based on data from 419. to 563. K.; AC
11.1377.EBBiddiscombe, Collerson, et al., 1963Based on data from 362. to 398. K.; AC
11.5352.N/ABrown and Smith, 1959Based on data from 337. to 390. K. See also Boublik, Fried, et al., 1984.; AC
11.5352.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) (kcal/mol)
    Tr = reduced temperature (T / Tc)

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Temperature (K) 298. to 410.
A (kcal/mol) 14.95
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 (atm)
    T = temperature (K)

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Temperature (K) A B C Reference Comment
295.8 to 391.04.540361351.555-93.34Kemme and Kreps, 1969 
391. to 479.4.384601254.502-105.246Hessel and Geiseler, 1965Coefficents calculated by NIST from author's data.
419.34 to 562.984.423501305.001-94.676Ambrose and Townsend, 1963, 2Coefficents calculated by NIST from author's data.
362.36 to 398.844.498221313.878-98.789Biddiscombe, Collerson, et al., 1963, 2Coefficents calculated by NIST from author's data.

Enthalpy of fusion

ΔfusH (kcal/mol) Temperature (K) Reference Comment
2.240184.5Counsell, Hales, et al., 1965DH
2.22183.9Acree, 1991AC
2.218183.9Parks, 1925DH

Entropy of fusion

ΔfusS (cal/mol*K) Temperature (K) Reference Comment
12.14184.5Counsell, Hales, et al., 1965DH
12.06183.9Parks, 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

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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 Comment
130.7200.MN/A 
120. CN/A 
53. MN/AValue at T = 303. K.
110. MButtery, Ling, et al., 1969 
140. MN/A 
120. 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

Quantity Value Units Method Reference Comment
IE (evaluated)9.99 ± 0.05eVN/AN/AL
Quantity Value Units Method Reference Comment
Proton affinity (review)188.6kcal/molN/AHunter and Lias, 1998HL
Quantity Value Units Method Reference Comment
Gas basicity181.4kcal/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
Δr375.3 ± 2.0kcal/molCIDCHaas and Harrison, 1993gas phase; Both metastable and 50 eV collision energy.; B
Δr375.4 ± 2.1kcal/molG+TSBartmess, Scott, et al., 1979gas phase; value altered from reference due to change in acidity scale; B
Δr375.0 ± 2.9kcal/molG+TSBoand, Houriet, et al., 1983gas phase; value altered from reference due to change in acidity scale; B
Quantity Value Units Method Reference Comment
Δr368.7 ± 2.1kcal/molH-TSHaas and Harrison, 1993gas phase; Both metastable and 50 eV collision energy.; B
Δr368.8 ± 2.0kcal/molIMREBartmess, Scott, et al., 1979gas phase; value altered from reference due to change in acidity scale; B
Δr368.4 ± 2.8kcal/molCIDCBoand, Houriet, et al., 1983gas phase; value altered from reference due to change in acidity scale; 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.

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]

Chermin H.A.G., 1961
Chermin H.A.G., Thermo data for petrochemicals. Part 28. Gaseous normal alcohols. The important thermo properties are presented for all the gaseous normal alcohols from methanol through n-decanol, Petrol. Refiner, 1961, 40 (4), 127-130. [all data]

Buckley E., 1967
Buckley E., Chemical equilibria. Part 2. Dehydrogenation of propanol and butanol, Trans. Faraday Soc., 1967, 63, 895-901. [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]

Dyatkina M.E., 1954
Dyatkina M.E., Thermodynamic functions of normal alcohols (propanol, butanol, ethylene glycol), Zh. Fiz. Khim., 1954, 28, 377. [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, 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, 1869-1875. [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]

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]

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]

Gates, Wood, et al., 1986
Gates, J.A.; Wood, R.H.; Cobos, J.C.; Casanova, C.; Roux, A.H.; Roux-Desgranges, G.; Grolier, J.-P.E., Densities and heat capacities of 1-butanol + n-decane from 298 K to 400 K, Fluid Phase Equilib., 1986, 27, 137-151. [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]

Naziev, Bashirov, et al., 1986
Naziev, Ya.M.; Bashirov, M.M.; Badalov, Yu.A., Experimental device for measurement of isobaric specific heat of electrolytes at elevated pressures, Inzh-Fiz. Zhur., 1986, 51(5), 789-795. [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]

Roux-Dexgranges, Grolier, et al., 1986
Roux-Dexgranges, G.; Grolier, J.-P.E.; Villamanan, M.A.; Casanova, C., Role of alcohol in microemulsions. III. Volumes and heat capacities in the continuious phase water-n-butanol-toluene of reverse micelles, Fluid Phase Equilibria, 1986, 25, 209-230. [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]

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]

Arutyunyan, Bagdasaryan, et al., 1981
Arutyunyan, G.S.; Bagdasaryan, S.S.; Kerimov, A.M., Experimental investigation of the isobaric heat capacity of n-propyl, n-butyl and n-amyl alcohols at different temperatures and pressures, Izv. Akad. Nauk Azerb. SSr, 1981, (6), 94-97. [all data]

Griigo'ev, Yanin, et al., 1979
Griigo'ev, B.A.; Yanin, G.S.; Rastorguev, Yu.L.; Thermophysical parameters of alcohols, Tr. GIAP, 54, 1979, 57-64. [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]

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

Trew and Watkins, 1933
Trew, V.C.G.; Watkins, G.M.C., Some physical properties of mixtures of certain organic liquids, Trans. Faraday Soc., 1933, 29, 1310-1318. [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]

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]

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, 2
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, 2
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
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Notes

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