1,4-Dioxane

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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
GT - Glushko Thermocenter, Russian Academy of Sciences, Moscow

Quantity Value Units Method Reference Comment
Δfgas-315.30 ± 0.80kJ/molCcrBystrm and Mansson, 1982Reanalyzed by Cox and Pilcher, 1970, Original value = -316.5 ± 0.9 kJ/mol; ALS
Δfgas-318. ± 2.kJ/molCcbSnelson and Skinner, 1961ALS
Quantity Value Units Method Reference Comment
gas299.91J/mol*KN/AStull D.R., 1969GT

Constant pressure heat capacity of gas

Cp,gas (J/mol*K) Temperature (K) Reference Comment
33.8550.Dorofeeva O.V., 1992p=1 bar. Selected values are in close agreement with statistical values calculated by [ Ellestad O.H., 1971, Thermodynamics Research Center, 1997]. Heat capacities calculated by [ Malherbe F.E., 1952] are 2-3 J/mol*K larger than those given here.; GT
41.06100.
51.71150.
63.63200.
84.31273.15
92.1 ± 1.5298.15
92.71300.
124.76400.
153.97500.
178.64600.
199.16700.
216.33800.
230.78900.
243.021000.
253.431100.
262.321200.
269.941300.
276.491400.
282.151500.

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-355.13 ± 0.86kJ/molCcrBystrm and Mansson, 1982ALS
Δfliquid-353.5 ± 0.8kJ/molCcbSnelson and Skinner, 1961ALS
Quantity Value Units Method Reference Comment
Δcliquid-2362.23 ± 0.99kJ/molCcrBystrm and Mansson, 1982Corresponding Δfliquid = -355.13 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS
Δcliquid-2363.9 ± 0.50kJ/molCcbSnelson and Skinner, 1961Corresponding Δfliquid = -353.4 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS
Δcliquid-2346.2kJ/molCcbRoth and Meyer, 1933Corrected for pressure and temperature; Corresponding Δfliquid = -371.1 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS
Δcliquid-2186.8kJ/molCcbHerz and Lorentz, 1929Corresponding Δfliquid = -530.57 kJ/mol (simple calculation by NIST; no Washburn corrections); ALS
Quantity Value Units Method Reference Comment
liquid196.6J/mol*KN/AJacobs and Parks, 1934Extrapolation below 90 K, 11.12 cal/mol*K.; DH

Constant pressure heat capacity of liquid

Cp,liquid (J/mol*K) Temperature (K) Reference Comment
149.65298.15Grolier, Roux-Desgranges, et al., 1993DH
150.57298.15Trejo, Costas, et al., 1991DH
149.489298.15Barta, Kooner, et al., 1989DH
150.65298.15Grolier, Inglese, et al., 1984DH
150.77298.15Inglese, Grolier, et al., 1984DH
149.73298.15Inglese, Castagnolo, et al., 1981DH
149.0298.Murthy and Subrahmanyam, 1979DH
149.298.15Bonner and Cerutti, 1976DH
140.2298.Conti, Gianni, et al., 1976DH
155.6298.Deshpande and Bhatagadde, 1971T = 298 to 318 K.; DH
147.9298.15Hyder Khan and Subrahmanyam, 1971T = 298; 313 K.; DH
147.9298.Subrahmanyam and Khan, 1969DH
152.97298.2Jacobs and Parks, 1934T = 92 to 299 K. Value is unsmoothed experimental datum.; DH
146.0291.Roth and Meyer, 1933T = 8 to 28°C.; DH
154.8296.Herz and Lorentz, 1929DH

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:
BS - Robert L. Brown and Stephen E. Stein
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, Chris Muzny director
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein
DRB - Donald R. Burgess, Jr.
AC - William E. Acree, Jr., James S. Chickos
DH - Eugene S. Domalski and Elizabeth D. Hearing
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
Tboil374.3 ± 0.8KAVGN/AAverage of 20 out of 21 values; Individual data points
Quantity Value Units Method Reference Comment
Tfus285. ± 1.KAVGN/AAverage of 17 out of 18 values; Individual data points
Quantity Value Units Method Reference Comment
Ttriple284.1KN/AJacobs and Parks, 1934, 2Crystal phase 1 phase; Uncertainty assigned by TRC = 0.2 K; TRC
Quantity Value Units Method Reference Comment
Tc587.3KN/ACristou, Young, et al., 1991Uncertainty assigned by TRC = 1. K; TRC
Tc588.15KN/AGlaser and Ruland, 1957Uncertainty assigned by TRC = 2. K; TRC
Tc588.KN/AKobe, Ravicz, et al., 1956Uncertainty assigned by TRC = 2. K; TRC
Tc585.15KN/AHojendahl, 1946Uncertainty assigned by TRC = 2. K; TRC
Quantity Value Units Method Reference Comment
Pc54.7155barN/AGlaser and Ruland, 1957Uncertainty assigned by TRC = 3.0398 bar; TRC
Pc52.10barN/AKobe, Ravicz, et al., 1956Uncertainty assigned by TRC = 0.6894 bar; TRC
Pc50.00barN/AHojendahl, 1946Uncertainty assigned by TRC = 0.70 bar; by extrapolation of vapor pressure to critical temperature; TRC
Quantity Value Units Method Reference Comment
Vc0.239l/molN/ACristou, Young, et al., 1991Uncertainty assigned by TRC = 0.008 l/mol; TRC
Vc0.239l/molN/AKobe, Ravicz, et al., 1956Uncertainty assigned by TRC = 0.004 l/mol; TRC
Quantity Value Units Method Reference Comment
ρc4.09mol/lN/AHojendahl, 1946Uncertainty assigned by TRC = 0.11 mol/l; TRC
Quantity Value Units Method Reference Comment
Δvap38. ± 4.kJ/molAVGN/AAverage of 7 values; Individual data points

Enthalpy of vaporization

ΔvapH (kJ/mol) Temperature (K) Method Reference Comment
34.16374.5N/AMajer and Svoboda, 1985 
38.300.AStephenson and Malanowski, 1987Based on data from 285. to 375. K.; AC
36.5350.N/ACastellari, Comelli, et al., 1984Based on data from 329. to 372. K.; AC
37.3308.N/AVinson and Martin, 1963Based on data from 293. to 398. K. See also Boublik, Fried, et al., 1984.; AC
35.8273.VGallaugher and Hibbert, 1937ALS
37.318.N/AHovorka, Schaefer, et al., 1936Based on data from 283. to 353. K.; AC

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
293. to 378.4.581351570.093-31.297Crenshaw, Cope, et al., 1938Coefficents calculated by NIST from author's data.

Enthalpy of sublimation

ΔsubH (kJ/mol) Temperature (K) Method Reference Comment
35.6255.AStull, 1947Based on data from 237. to 272. K.; AC

Enthalpy of fusion

ΔfusH (kJ/mol) Temperature (K) Reference Comment
12.84284.1Domalski and Hearing, 1996AC
11.880283.2Roth and Meyer, 1933DH

Entropy of fusion

ΔfusS (J/mol*K) Temperature (K) Reference Comment
41.9283.2Roth and Meyer, 1933DH

Entropy of fusion

ΔfusS (J/mol*K) Temperature (K) Reference Comment
8.79272.9Domalski and Hearing, 1996CAL
45.19284.1

Enthalpy of phase transition

ΔHtrs (kJ/mol) Temperature (K) Initial Phase Final Phase Reference Comment
2.351272.9crystaline, IIcrystaline, IJacobs and Parks, 1934DH
12.845284.1crystaline, IliquidJacobs and Parks, 1934DH

Entropy of phase transition

ΔStrs (J/mol*K) Temperature (K) Initial Phase Final Phase Reference Comment
8.6272.9crystaline, IIcrystaline, IJacobs and Parks, 1934DH
45.2284.1crystaline, IliquidJacobs and Parks, 1934DH

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
140. QN/A missing citation give several references for the Henry's law constants but don't assign them to specific species.
140. MN/AValue at T = 303. K.
220. MN/A 
210. XN/AValue given here as quoted by missing citation.
200.5800.MN/A 

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:
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

View reactions leading to C4H8O2+ (ion structure unspecified)

Quantity Value Units Method Reference Comment
IE (evaluated)9.19 ± 0.01eVN/AN/AL
Quantity Value Units Method Reference Comment
Proton affinity (review)797.4kJ/molN/AHunter and Lias, 1998HL
Quantity Value Units Method Reference Comment
Gas basicity770.0kJ/molN/AHunter and Lias, 1998HL

Ionization energy determinations

IE (eV) Method Reference Comment
9.19 ± 0.01PIPECOFraser-Monteiro, Fraser-Monteiro, et al., 1982LBLHLM
9.13 ± 0.03PIWatanabe, Nakayama, et al., 1962RDSH
9.4PEBieri, Asbrink, et al., 1982Vertical value; LBLHLM
9.43PEKimura, Katsumata, et al., 1981Vertical value; LLK
9.41PEKobayashi and Nagakura, 1973Vertical value; LLK
9.3 ± 0.1SIGol'denfel'd, Korostyshevskii, et al., 1973Vertical value; LLK
9.43PESweigart and Turner, 1972Vertical value; LLK

Appearance energy determinations

Ion AE (eV) Other Products MethodReferenceComment
CHO+11.60 ± 0.10C3H7OPIPECOFraser-Monteiro, Fraser-Monteiro, et al., 1982T = 298K; LBLHLM
CH2O+11.41 ± 0.05C3H6OPIPECOFraser-Monteiro, Fraser-Monteiro, et al., 1982T = 298K; LBLHLM
CH3O+11.35 ± 0.10C3H5OPIPECOFraser-Monteiro, Fraser-Monteiro, et al., 1982T = 298K; LBLHLM
C2H3O+11.96 ± 0.10C2H5OPIPECOFraser-Monteiro, Fraser-Monteiro, et al., 1982T = 298K; LBLHLM
C2H3O+12.92?EICollin and Conde, 1966RDSH
C2H4+11.90 ± 0.102CH2O/C2H4O2PIPECOFraser-Monteiro, Fraser-Monteiro, et al., 1982T = 298K; LBLHLM
C2H4O+10.39 ± 0.05C2H4OPIPECOFraser-Monteiro, Fraser-Monteiro, et al., 1982T = 298K; LBLHLM
C2H4O+10.90?EICollin and Conde, 1966RDSH
C2H5O+10.46 ± 0.05C2H3OPIPECOFraser-Monteiro, Fraser-Monteiro, et al., 1982T = 298K; LBLHLM
C3H5O+11.20 ± 0.10CH3OPIPECOFraser-Monteiro, Fraser-Monteiro, et al., 1982T = 298K; LBLHLM
C3H6O+10.65CH2OPIPECOFraser-Monteiro, Fraser-Monteiro, et al., 1982T = 0K; LBLHLM
C3H6O+10.56 ± 0.10CH2OPIPECOFraser-Monteiro, Fraser-Monteiro, et al., 1982T = 298K; LBLHLM
C3H6O+11.CH2OEICollin and Conde, 1966RDSH
C4H7O2+10.95HEICollin and Conde, 1966RDSH

Ion clustering data

Go To: Top, Gas phase thermochemistry data, Condensed phase thermochemistry data, Phase change data, Henry's Law data, Gas phase ion energetics 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 compiled as indicated in comments:
M - Michael M. Meot-Ner (Mautner) and Sharon G. Lias
RCD - 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

C3H7O+ + 1,4-Dioxane = (C3H7O+ • 1,4-Dioxane)

By formula: C3H7O+ + C4H8O2 = (C3H7O+ • C4H8O2)

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

Quantity Value Units Method Reference Comment
Δr126.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, Keesee and Castleman, 1986; M
Quantity Value Units Method Reference Comment
Δr126.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, Keesee and Castleman, 1986; M
Quantity Value Units Method Reference Comment
Δr87.9kJ/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, Keesee and Castleman, 1986; M

C4H9O2+ + 1,4-Dioxane = (C4H9O2+ • 1,4-Dioxane)

By formula: C4H9O2+ + C4H8O2 = (C4H9O2+ • C4H8O2)

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

Quantity Value Units Method Reference Comment
Δr129.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, Keesee and Castleman, 1986; M
Quantity Value Units Method Reference Comment
Δr132.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, Keesee and Castleman, 1986; M
Quantity Value Units Method Reference Comment
Δr90.0kJ/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, Keesee and Castleman, 1986; M

Sodium ion (1+) + 1,4-Dioxane = (Sodium ion (1+) • 1,4-Dioxane)

By formula: Na+ + C4H8O2 = (Na+ • C4H8O2)

Free energy of reaction

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

Mass spectrum (electron ionization)

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, 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 NIST Mass Spectrometry Data Center, 1990.
NIST MS number 118696

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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.

Bystrm and Mansson, 1982
Bystrm, K.; Mansson, M., Enthalpies of formation of some cyclic 1,3- and 1,4-Di- and poly-ethers: Thermochemical strain in the -O-C-O and -O-C-C-O- groups, J. Chem. Soc. Perkin Trans. 2, 1982, 565. [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]

Snelson and Skinner, 1961
Snelson, A.; Skinner, H.A., Heats of combustion: sec-propanol, 1,4-dioxan, 1,3-dioxan and tetrahydropyran, Trans. Faraday Soc., 1961, 57, 2125-2131. [all data]

Stull D.R., 1969
Stull D.R., Jr., The Chemical Thermodynamics of Organic Compounds. Wiley, New York, 1969. [all data]

Dorofeeva O.V., 1992
Dorofeeva O.V., Ideal gas thermodynamic properties of oxygen heterocyclic compounds. Part 2. Six-membered, seven-membered and eight-membered rings, Thermochim. Acta, 1992, 200, 121-150. [all data]

Ellestad O.H., 1971
Ellestad O.H., The vibrational spectra of 1,4-dioxan-d0 and 1,4-dioxan-d8, Spectrochim. Acta, 1971, A27, 1025-1048. [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]

Malherbe F.E., 1952
Malherbe F.E., The infrared and Raman spectra of p-dioxane, J. Am. Chem. Soc., 1952, 74, 4408-4410. [all data]

Roth and Meyer, 1933
Roth, W.A.; Meyer, I., Einige physikalisch-chemische konstanten des dioxans, Z. Electrochem., 1933, 39, 35-37. [all data]

Herz and Lorentz, 1929
Herz, W.; Lorentz, E., Physikalisch-chemische Untersuchungen an Dioxan, Z. Phys. Chem., 1929, 140, 406-422. [all data]

Jacobs and Parks, 1934
Jacobs, C.J.; Parks, G.S., Thermal data on organic compounds. XIV. Some heat capacity, entropy and free energy data for cyclic substances, J. Am. Chem. Soc., 1934, 56, 1513-1517. [all data]

Grolier, Roux-Desgranges, et al., 1993
Grolier, J.-P.E.; Roux-Desgranges, G.; Berkane, M.; Jimenez, E.; Wilhelm, E., Heat capacities and densities of mixtures of very polar substances 2. Mixtures containing N,N-dimethylformamide, J. Chem. Thermodynam., 1993, 25(1), 41-50. [all data]

Trejo, Costas, et al., 1991
Trejo, L.M.; Costas, M.; Patterson, D., Excess heat capacity of organic mixtures, Internat. DATA Series, Selected Data Mixt., 1991, Ser. [all data]

Barta, Kooner, et al., 1989
Barta, L.; Kooner, Z.S.; Hepler, L.G.; Roux-Desgranges, G.; Grolier, J.-P.E., Thermodynamics of complex formation in chloroform and 1,4-dioxane, Can. J. Chem., 1989, 67, 1225-1229. [all data]

Grolier, Inglese, et al., 1984
Grolier, J.-P.E.; Inglese, A.; Wilhelm, E., Excess molar heat capacities of (1,4-dioxane + an n-alkane): an unusual composition dependence, J. Chem. Thermodynam., 1984, 16, 67-71. [all data]

Inglese, Grolier, et al., 1984
Inglese, A.; Grolier, J.-P.E.; Wilhelm, E., Excess volumes and excess heat capacities of oxane + cyclohexane and 1,4-dioxane + cyclohexane, Fluid Phase Equilibria, 1984, 15, 287-294. [all data]

Inglese, Castagnolo, et al., 1981
Inglese, A.; Castagnolo, M.; Dell'Atti, A.; DeGiglio, A., Thermochim. Acta, 1981, 77-87. [all data]

Murthy and Subrahmanyam, 1979
Murthy, N.M.; Subrahmanyam, S.V., Behavior of excess heat capacity of the water + p-dioxane system, Indian J. Pure Appl. Phys., 1979, 17(9), 620-622. [all data]

Bonner and Cerutti, 1976
Bonner, O.D.; Cerutti, P.J., The partial molar heat capacities of some solutes in water and deuterium oxide, J. Chem. Thermodynam., 1976, 8, 105-111. [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]

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]

Hyder Khan and Subrahmanyam, 1971
Hyder Khan, V.; Subrahmanyam, S.V., Excess thermodynamic functions of the systems: benzene + p-xylene and benzene + p-dioxan, Trans. Faraday Soc., 1971, 67, 2282-2291. [all data]

Subrahmanyam and Khan, 1969
Subrahmanyam, S.V.; Khan, V.H., Thermodynamics of the system benzene - p-dioxane, Curr. Sci., 1969, 38, 510-511. [all data]

Jacobs and Parks, 1934, 2
Jacobs, C.J.; Parks, G.S., Thermal data on organic compounds. XIV. Some heat capacity, entropy and free energy data for cyclic substances, J. Am. Chem. Soc., 1934, 56, 1513-17. [all data]

Cristou, Young, et al., 1991
Cristou, G.; Young, C.L.; Svejda, P., Fluid Phase Equilibria, 1991, 67, 45-53. [all data]

Glaser and Ruland, 1957
Glaser, F.; Ruland, H., Untersuchungsen über dampfdruckkurven und kritische daten einiger technisch wichtiger organischer substanzen, Chem. Ing. Techn., 1957, 29, 772. [all data]

Kobe, Ravicz, et al., 1956
Kobe, K.A.; Ravicz, A.E.; Vohra, S.P., Critical Properties and Vapor Pressures of Some Ethers and Heterocyclic Compounds, J. Chem. Eng. Data, 1956, 1, 50. [all data]

Hojendahl, 1946
Hojendahl, K., Dielectric Constant, Viscosity, Surface Tension, and Critical Data of Boron Tribromide, Dioxane, and Ethylene Dichloride, Mat.-Fys. Medd. - K. Dan. Vidensk. Selsk., 1946, 24, 1. [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]

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]

Castellari, Comelli, et al., 1984
Castellari, Carlo; Comelli, Fabio; Francesconi, Romolo, Vapor-liquid equilibria in binary systems containing 1,3-dioxolane at isobaric conditions. 4. Binary mixtures of 1,3-dioxolane with 1,4-dioxane and 1,1,2,2-tetrachloroethane, J. Chem. Eng. Data, 1984, 29, 2, 126-128, https://doi.org/10.1021/je00036a008 . [all data]

Vinson and Martin, 1963
Vinson, Carl G.; Martin, Joseph J., Heat of Vaporization and Vapor Pressure of 1,4-Dioxane., J. Chem. Eng. Data, 1963, 8, 1, 74-75, https://doi.org/10.1021/je60016a021 . [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]

Gallaugher and Hibbert, 1937
Gallaugher, A.F.; Hibbert, H., Studies on reactions relating to carbohydrates and polysaccharides. LV. Vapor pressures of the polyethylene glycols and their derivatives, J. Am. Chem. Soc., 1937, 59, 2521-2525. [all data]

Hovorka, Schaefer, et al., 1936
Hovorka, Frank; Schaefer, Ralph A.; Dreisbach, Dale, The System Dioxane and Water, J. Am. Chem. Soc., 1936, 58, 11, 2264-2267, https://doi.org/10.1021/ja01302a051 . [all data]

Crenshaw, Cope, et al., 1938
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Notes

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