Ethyl ether

Data at NIST subscription sites:

NIST subscription sites provide data under the NIST Standard Reference Data Program, but require an annual fee to access. The purpose of the fee is to recover costs associated with the development of data collections included in such sites. Your institution may already be a subscriber. Follow the links above to find out more about the data in these sites and their terms of usage.


Critical temperature

Go To: Top, 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

Tc (K) Reference Comment
466.7Majer and Svoboda, 1985 
466.7Young, 1975Uncertainty assigned by TRC = 0.3 K; TRC
466.74Ambrose, Sprake, et al., 1972Uncertainty assigned by TRC = 0.04 K; Tc by A.C.Zawisza, 1967-337; TRC
466.7Ratzsh, 1970Uncertainty assigned by TRC = 0.4 K; TRC
466.70Zawisza, 1967Uncertainty assigned by TRC = 0.4 K; TRC
466.8Stryjek and Kreglewski, 1965Uncertainty assigned by TRC = 0.6 K; TRC
465.8Kobe, Ravicz, et al., 1956Uncertainty assigned by TRC = 1. K; TRC
466.56Kay and Donham, 1955Uncertainty assigned by TRC = 0.4 K; TRC
465.5Fischer and Reichel, 1943Uncertainty assigned by TRC = 2. K; TRC
466.50Schroeer, 1929Uncertainty assigned by TRC = 0.4 K; TRC
467.8Schroeer, 1929, 2Uncertainty assigned by TRC = 1. K; TRC
466.76Wilip, 1924Uncertainty assigned by TRC = 0.4 K; TRC
466.Audant, 1920Uncertainty assigned by TRC = 2. K; 60297; TRC
467.0Prins and Scheffer, 1913Uncertainty assigned by TRC = 0.6 K; TRC
467.0Young, 1910Uncertainty assigned by TRC = 0.4 K; TRC
466.6Schamhardt, 1908Uncertainty assigned by TRC = 0.8 K; TRC
467.5Centerszwer and Pakalneet, 1906Uncertainty assigned by TRC = 0.6 K; from disappearance of meniscus, mean for values for heating and cooling; TRC
466.76Travers and Usher, 1906Uncertainty assigned by TRC = 0.5 K; by disappearance of meniscus; TRC
466.Smits, 1905Uncertainty assigned by TRC = 4. K; TRC
467.6Centnerszwer, 1904Uncertainty assigned by TRC = 0.5 K; max. temp. of disappearance of meniscus for various fillings; TRC
466.76Galitzine and Wilip, 1901Uncertainty assigned by TRC = 0.4 K; TRC
467.9Von Hirsch, 1900Uncertainty assigned by TRC = 1. K; TRC
466.8De Vries, 1895Uncertainty assigned by TRC = 1. K; TRC
470.Battelli, 1892Uncertainty assigned by TRC = 3. K; TRC
472.5Heilbron, 1891Uncertainty assigned by TRC = 5. K; TRC; Data excluded from overall average
466.7Schmidt, 1891Uncertainty assigned by TRC = 1. K; TRC
464.0Galitzin, 1890Uncertainty assigned by TRC = 2. K; TRC
467.Ramsay and Young, 1887Uncertainty assigned by TRC = 2. K; TRC
468.7Ramsay, 1881Uncertainty assigned by TRC = 2. K; TRC
463.2Sajots, 1879Uncertainty assigned by TRC = 3. K; TRC

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, Critical temperature, Notes

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

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]

Young, 1975
Young, C.L., Gas-liquid critical properties. Diethyl ether-n-hexane system, Int. DATA Ser., Sel. Data Mixtures, Ser. A, 1975, No. 1, 70. [all data]

Ambrose, Sprake, et al., 1972
Ambrose, D.; Sprake, C.H.S.; Townsend, R., Thermodynamic properties of organic oxygen compounds XXIX. The vapor pressure of diethyl ether, J. Chem. Thermodyn., 1972, 4, 247. [all data]

Ratzsh, 1970
Ratzsh, M.T., Z. Phys. Chem. Leipzig, 1970, 243, 212-9. [all data]

Zawisza, 1967
Zawisza, A.C., High pressure phase equilibriums and the compressibility of the sulfur dioxide - diethyl ether system, Bull. Acad. Pol. Sci., Ser. Sci. Chim., 1967, 15, 291-7. [all data]

Stryjek and Kreglewski, 1965
Stryjek, R.; Kreglewski, A., The Second Virial Coefficients of Maseous Mixtures 1, The Diethyl Ether- Sulfur Dioxide System, Bull. Acad. Pol. Sci., Ser. Sci. Chim., 1965, 13, 201-7. [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]

Kay and Donham, 1955
Kay, W.B.; Donham, W.E., Liquid-Vapor Equilibrium in the Isobutyl Alcohol-Butanol, Methanol- Butanol, and Diethyl Ether-Butanol Systems, Chem. Eng. Sci., 1955, 4, 1-16. [all data]

Fischer and Reichel, 1943
Fischer, R.; Reichel, T., Determination of the Critical Temperature BY Means of the Micro Melting-Point Apparatus, Mikrochem. Ver. Mikrochim. Acta, 1943, 31, 102. [all data]

Schroeer, 1929
Schroeer, E., The Critical State II. Limiting Curve of Ethyl Ether, Z. Phys. Chem., Abt. A, 1929, 140, 241-53. [all data]

Schroeer, 1929, 2
Schroeer, E., The Critical State III. Behaviour of Ethyl Ether Under Isothermal Compression in the Critical and Hypercritical Region, Z. Phys. Chem., Abt. A, 1929, 140, 379-90. [all data]

Wilip, 1924
Wilip, J., , Eesti Vabariigi Tartu Ulik. Toim. A 6(2), 74pp, 1924. [all data]

Audant, 1920
Audant, Contributions to the study at the critical state of ethyl ether., C. R. Hebd. Seances Acad. Sci., 1920, 170, 1573-5. [all data]

Prins and Scheffer, 1913
Prins, A.; Scheffer, F.E.C., J. Phys. Chem., 1913, 84, 827. [all data]

Young, 1910
Young, S., The Internal Heat of Vaporization constants of thirty pure substances, Sci. Proc. R. Dublin Soc., 1910, 12, 374. [all data]

Schamhardt, 1908
Schamhardt, , Thesis, Amsterdam, 1908. [all data]

Centerszwer and Pakalneet, 1906
Centerszwer, M.; Pakalneet, A., The critical pressure of solutions, Z. Phys. Chem., Stoechiom. Verwandtschaftsl., 1906, 55, 303. [all data]

Travers and Usher, 1906
Travers, M.W.; Usher, F.L., The behavior of certain substance at the critical point, Z. Phys. Chem., Stoechiom. Verwandtschaftsl., 1906, 57, 365-81. [all data]

Smits, 1905
Smits, A., On the Phenomenon, which arises, in Binary Mixtures when the Fold-Point Curve Intersects the Solubility Curve, Z. Phys. Chem., Stoechiom. Verwandtschaftsl., 1905, 52, 587. [all data]

Centnerszwer, 1904
Centnerszwer, M., An Application of the Method of Cailletet and Mathias to Determine Critical Volume., Z. Phys. Chem., Stoechiom. Verwandtschaftsl., 1904, 49, 199. [all data]

Galitzine and Wilip, 1901
Galitzine, B.; Wilip, J., Bull. Acad. Pet., 1901, 1901, No. 3, 117. [all data]

Von Hirsch, 1900
Von Hirsch, Ann. Phys. (Leipzig), 1900, 1, 655. [all data]

De Vries, 1895
De Vries, E.C., Arch. Neerl. Sci. Exactes Nat., 1895, 28, 215. [all data]

Battelli, 1892
Battelli, A., Ann. Chim. Phys., 1892, 25, 38. [all data]

Heilbron, 1891
Heilbron, E., Summary of the Critical Data Up To Now on Liquids., Z. Phys. Chem., Stoechiom. Verwandtschaftsl., 1891, 1, 601-13. [all data]

Schmidt, 1891
Schmidt, G.C., The Critical Temperature of Liquid Mixtures, Justus Liebigs Ann. Chem., 1891, 266, 266-92. [all data]

Galitzin, 1890
Galitzin, Ann. Phys. (Leipzig), 1890, 41, 588. [all data]

Ramsay and Young, 1887
Ramsay, W.; Young, S., On evaporation and dissociation part III a study of the thermal properties of ethyl oxide, Philos. Trans. R. Soc. London, A, 1887, 178, 57-93. [all data]

Ramsay, 1881
Ramsay, W., Proc. R. Soc. London, 1881, 31, 194-205. [all data]

Sajots, 1879
Sajots, W., Vapor Pressures of Saturated Vapors at High Temperatures., Beibl. Ann. Phys., 1879, 3, 741-3. [all data]


Notes

Go To: Top, Critical temperature, References