Ethanol, 2,2'-oxybis-

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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
AC - William E. Acree, Jr., James S. Chickos
ALS - Hussein Y. Afeefy, Joel F. Liebman, and Stephen E. Stein

Quantity Value Units Method Reference Comment
Tboil519. ± 3.KAVGN/AAverage of 6 values; Individual data points
Quantity Value Units Method Reference Comment
Tfus265.4KN/AAnonymous, 1958Uncertainty assigned by TRC = 0.6 K; TRC
Tfus263.05KN/AGallaugher and Hibbert, 1936Uncertainty assigned by TRC = 0.5 K; TRC
Tfus262.80KN/ARinkenbach, 1927Uncertainty assigned by TRC = 0.1 K; TRC
Quantity Value Units Method Reference Comment
Tc753.KN/ANikitin, Pavlov, et al., 1995Uncertainty assigned by TRC = 4. K; TRC
Tc723.5KN/AAnselme and Teja, 1990Uncertainty assigned by TRC = 50. K; Tc > 723.5 K, which was observed with decomposition; TRC
Tc680.KN/AStephens and Tamplin, 1979Uncertainty assigned by TRC = 20. K; TC data from Union Carbide Corp.; TRC
Quantity Value Units Method Reference Comment
Pc47.70barN/ANikitin, Pavlov, et al., 1995Uncertainty assigned by TRC = 0.50 bar; TRC

Reduced pressure boiling point

Tboil (K) Pressure (bar) Reference Comment
406.20.019Weast and Grasselli, 1989BS

Enthalpy of vaporization

ΔvapH (kJ/mol) Temperature (K) Method Reference Comment
66.5413.TGAAl-Najjar and Al-Sammerrai, 2007Based on data from 373. - 453. K.; AC
66.9 ± 0.3420.EBSteele, Chirico, et al., 2002Based on data from 410. - 539. K.; AC
63.1 ± 0.3460.EBSteele, Chirico, et al., 2002Based on data from 410. - 539. K.; AC
59.2 ± 0.3500.EBSteele, Chirico, et al., 2002Based on data from 410. - 539. K.; AC
55.1 ± 0.5540.EBSteele, Chirico, et al., 2002Based on data from 410. - 539. K.; AC
59.8379.AStephenson and Malanowski, 1987Based on data from 364. - 518. K.; AC
66.8427.N/AAmbrose and Hall, 1981Based on data from 412. - 513. K. See also Boublik, Fried, et al., 1984.; AC
57.3 ± 5.9273.VGallaugher and Hibbert, 1937Reanalyzed by Pedley, Naylor, et al., 1986, Original value = 52.30 kJ/mol; ALS
66.57523.VRinkenbach, 1927, 2ALS
69.2418.N/ARinkenbach, 1927, 3Based on data from 403. - 513. K. See also Boublik, Fried, et al., 1984.; AC

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:


References

Go To: Top, Phase change data, Notes

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

Anonymous, 1958
Anonymous, R., , Am. Pet. Inst. Res. Proj. 45, Ohio State Univ., 1958. [all data]

Gallaugher and Hibbert, 1936
Gallaugher, A.F.; Hibbert, H., Studies on reactions relating to carbohydrates and polysaccharides: xlix molecular weight, molar refraction, freezing point and other properties of the polyethylene glycols and their derivatives, J. Am. Chem. Soc., 1936, 58, 813. [all data]

Rinkenbach, 1927
Rinkenbach, W.H., Properties of Diethylene Glycol, Ind. Eng. Chem., 1927, 19, 475-6. [all data]

Nikitin, Pavlov, et al., 1995
Nikitin, E.D.; Pavlov, P.A.; Popov, A.P., (Gas + liquid) critical temperatures and pressures of polyethene glycols for HOCH2CH2OH to H(OCH2CH2)v.apprxeq.13.2OH, J. Chem. Thermodyn., 1995, 27, 43-51. [all data]

Anselme and Teja, 1990
Anselme, M.J.; Teja, A.S., The critical properties of rapidly reacting substances, AIChE Symp. Ser., 1990, 86, 279, 128-32. [all data]

Stephens and Tamplin, 1979
Stephens, M.A.; Tamplin, W.S., Saturated Liquid SPecific Heats of Ethylene GLycol Homologues, J. Chem. Eng. Data, 1979, 24, 81-2. [all data]

Weast and Grasselli, 1989
CRC Handbook of Data on Organic Compounds, 2nd Editon, Weast,R.C and Grasselli, J.G., ed(s)., CRC Press, Inc., Boca Raton, FL, 1989, 1. [all data]

Al-Najjar and Al-Sammerrai, 2007
Al-Najjar, Hazim; Al-Sammerrai, Dhoaib, Thermogravimetric determination of the heat of vaporization of some highly polar solvents, J. Chem. Technol. Biotechnol., 2007, 37, 3, 145-152, https://doi.org/10.1002/jctb.280370302 . [all data]

Steele, Chirico, et al., 2002
Steele, W.V.; Chirico, R.D.; Cowell, A.B.; Knipmeyer, S.E.; Nguyen, A., Thermodynamic Properties and Ideal-Gas Enthalpies of Formation for Methyl Benzoate, Ethyl Benzoate, ( R )-(+)-Limonene, tert -Amyl Methyl Ether, trans -Crotonaldehyde, and Diethylene Glycol, J. Chem. Eng. Data, 2002, 47, 4, 667-688, https://doi.org/10.1021/je0100847 . [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 and Hall, 1981
Ambrose, D.; Hall, D.J., Thermodynamic properties of organic oxygen compounds L. The vapour pressures of 1,2-ethanediol (ethylene glycol) and bis(2-hydroxyethyl) ether (diethylene glycol), The Journal of Chemical Thermodynamics, 1981, 13, 1, 61-66, https://doi.org/10.1016/S0021-9614(81)80009-2 . [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]

Pedley, Naylor, et al., 1986
Pedley, J.B.; Naylor, R.D.; Kirby, S.P., Thermochemical Data of Organic Compounds, Chapman and Hall, New York, 1986, 1-792. [all data]

Rinkenbach, 1927, 2
Rinkenbach, Wm.H., Properties of Diethylene Glycol, Ind. Eng. Chem., 1927, 19, 474-475. [all data]

Rinkenbach, 1927, 3
Rinkenbach, Wm.H., Properties of Diethylene Glycol 1, Ind. Eng. Chem., 1927, 19, 4, 474-476, https://doi.org/10.1021/ie50208a017 . [all data]


Notes

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