Abstract
Guggenheim [1] has defined a class of liquid solutions as “simple mixtures” for which the equations for binary solutions are given as
Here γ is the liquid-phase activity coefficient, x is the mole fraction in the liquid phase, and the subscripts i and k denote the solute and the solvent, respectively. Guggenheim indicates that w is independent of x but will in general depend on T and P. In addition, he states “we are introducing the new name simple mixtures for mixtures conforming” to the above equations “and we emphasize that no restriction is placed on the temperature dependence of w.” He also notes that simple mixtures are important because their behavior is one of the simplest conceivable after ideal mixtures either from a mathematical or from a physical aspect; that many binary mixtures show a behavior which can be represented either accurately or approximately by the relationships for simple mixtures; and that statistical theory predicts that a mixture of two kinds of nonpolar molecules of similar shape and similar size should obey certain laws to which the relations for simple mixtures are a useful approximation. The relations for simple mixtures, as defined above, were first described by Porter in 1920 and then used by Heitler in 1926 to develop the model of liquids now generally recognized as the “quasi-crystalline” model. These relationships have also been used to correlate experimental measurements on various mixtures, especially by Hildebrand [2]. Guggenheim notes in passing that it was assumed by Heitler and subsequently generally accepted that the value of w should be independent of temperature but that this by no means followed from the quasi-crystalline model used in the derivation of the relation. Shortly thereafter, according to Guggenheim, Hildebrand [3] “defined a class of mixtures as regular solutions when S E = 0. It is doubtful whether a mixture, other than an ideal one, can be accurately regular. Nevertheless, the conception of a regular solution, as defined by Hildebrand, can be useful as a basis of comparison for real mixtures. Subsequently, Hildebrand used Heitler’s formulae with w independent of temperature to represent the properties of many regular solutions. Others came to associate these formulae and the model on which they were based with the name regular.“ In a subsequent publication Hildebrand [4] insisted that the term regular be restricted to his original definition of SE = O. In conformity with this preference Guggenheim introduced a new term of “simple mixtures” for mixtures conforming to (1) and (2).
Paper presented at 67th National AIChE Meeting, Atlanta, Georgia, Feb. 15–18, 1970.
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References
I. E. A. Guggenheim, Thermodynamics, An Advanced Treatment for Chemists and Physicists, 3rd ed., North-Holland Publishing Co., Amsterdam, Holland (1957), pp. 166, 184–185, 246, 250–252, 259, 277, 299.
J. H. Hildebrand and R. L. Scott, The Solubility of Nonelectrolytes, 3rd ed. (1950) supplemented, Dover Publications, New York (1964), pp. vi—vii, 17–19, 35, 46–47, 67, 90–92, 120–123, 160.
J. H. Hildebrand, J. Am. Chem. Soc., 51:66 (1929); see equations (7) and (8) and conclusions 1 and 2.
J. H. Hildebrand, Nature, 168: 868 (1951).
R. E. Latimer, AIChEJ., 3 (1):75 (1957), points 1, 2, 3.
R. E. Latimer, unpublished reports, Linde Co. (Mar. 4, 1957—Jan. 14, 1958), points 5, 9a, 11, 13a, 16, 18, 19, 20, 21, 23, 24, 25.
R. E. Latimer, “Liquid-Phase Activity Coefficients at 15 to 273°K,” Preprint 43b, addenda and errata sheet, presented at 67th National AIChE Meeting, Atlanta, Feb. 15–18, 1970, points 1 thru 40. (Copies available from author.)
J. H. Hildebrand, personal communication (Mar. 5, 1970 ).
J. K. H. Inglis, Phil. Mag.,11:640 (1906), points 1, 3.
I. Burn and F. Din, Trans. Faraday Soc.,58 (7): 1341 (1962), point 1.
G. B. Narinskii, Kislorod,10 (3):9 (1957); J. Phys. Chem. (USSR),34:1778 (1960), point 1.
G. M. Wilson, P. M. Silverberg, and M. G. Zellner, in: International Advances in Cryogenic Engineering, Springer Science+Business Media New York (1965), p. 192; USAF Aero Propulsion Lab. Tech. Doc. Rpt. 64–64 (Apr. 1964), OTS, US Dept. of Commerce, points 1, 2, 3.
R. E. Latimer, in: International Advances in Cryogenic Engineering, Springer Science+Business Media New York (1965), p. 208, points 1, 2.
R. E. Latimer, Chem. Eng. Progr., 63 (2):35 (1967); ibid., 63 (3): 17 (1967); Preprint 41A, presented at 59th Annual AIChE Meeting, Detroit, Dec. 4–8, 1966, points I, 2, 3, 8, 27.
G. Holst and L. Hamburger, Z. physik. Chemie,91:513 (1916), point 2.
B. F. Dodge and A. K. Dunbar, J. Am. Chem. Soc.,49:591 (1927), point 3.
G. T. Armstrong, J. M. Goldstein, and D. E. Roberts, NBS J. Res.,55 (5):265 (1955), point 3.
G. H. Hanson, R. J. Hogan, F. N. Ruehlen, and M. R. Cines, Chem. Eng. Progr. Symp. Ser.,49 (6):37 (1953), point 4.
H. Cheung and D. 1-J Wang, Ind. Eng. Chem. Fund.,3 (4):355 (1964), points 5, 6a, 9a, 13a, 19, 22, 23, 25, 26.
A. M. Bekelman, unpublished experimental data, Linde Co. (1957), points 5, 9a, 11, 13a, 16, 18, 19, 20, 21, 23, 24, 25.
M. Ruhemann, Separation of Gases,2nd ed., Oxford Press (1949), pp. 60–61, point 7.
W. G. Fastowsky and J. G. Gurwitsch, Acta Physicochimica (USSR),11 (6):883 (1939), point 8.
A. Toyama, P. S. Chappelear, T. W. Leland, and R. Kobayashi, in: Advances in Cryogenic Engineering, Vol. 7, Springer Science+Business Media New York (1962), p. 125, point 6b.
M. Guter, D. M. Newitt, and M. Ruhemann, Proc. Roy. Soc. (A), 176:140 (1940); L. M. Volova, Zh. Fi:, Khim. 14:268 (1940), point 10.
O. T. Bloomer and J. D. Parent, I.G.T. Res. Bull. 17, p. 5 (Apr. 1952), point 9b.
C. K. Heck and P. L. Barrick, in: Advances in Cryogenic Engineering, Vol. 11,Springer Science+Business Media New York (1966), p. 349, point 12.
O. T. Bloomer, D. C. Gami, and J. D. Parent, I.G.T. Res. Bull. 22, p. 4 (July 1953), point 14.
W. B. Streett, R. E. Sonntag, and G. J. Van Wylen, J. Chem. Phys.,40 (5):1390 (1964), points 15a, 156.
C. K. Fleck and P. L. Barrick, in: Advances in Cryogenic Engineering, Vol. 11,Springer Science+Business Media New York (1967), p. 714, point 17.
W. B. Streett, Cryogenics,5 (1):27 (1965), point 27.
W. W. Akers, R. E. Kelley, and T. G. Lipscomb, Ind. Eng. Chem.,46 (12):2535 (1954), point 28.
M. Ruhemann and N. Zinn, Phys. Z. (USSR),12:389 (1937), point 29.
W. W. Akers, J. F. Burns, and W. R. Fairchild, Ind. Eng. Chem.,46 (12):2531 (1954), point 13b.
T. T. H. Verschoyle, Phil. Trans. Roy. Soc. (A), 130:189 (1931); F. Steckel and N. Zinn, Zh. Khim. Prom.,16:8 (1939); M. Ruhemann and N. Zinn, Phys. Z. (USSR),12:389 (1937), point 30.
W. B. Streett, J. Chem. Phys.,42 (2):500 (1965), points 31a, 31h.
A. L. Benham and D. L. Katz, AIChE J.,3 (l):33 (1957), point 32.
W. B. Streett and C. H. Jones, in: Advances in Cryogenic Engineering, Vol. 11, Springer Science+Business Media New York (1966), p. 356, points 33a, 33b.
J. C. Mullins and W. T. Ziegler, in: International Advances in Cryogenic Engineering, Springer Science+Business Media New York (1965), p. 171, points 34, 39.
G. H. Zenner and L. I. Dana, Chem. Eng. Progr. Symp. Ser.,59 (44):36 (1963), points 35, 36.
M. J. Hiza, C. K. Heck, and A. J. Kidnay, in: Advances in Cryogenic Engineering, Vol. 13,Springer Science+Business Media New York (1968), p. 343, point 37.
W. E. DeVaney, B. J. Dalton, and J. C. Meeks, Jr., J. Chem. Eng. Data,8 (4):473 (1963), point 38.
C. K. Heck and M. J. Hiza, AIChE J.,13 (3):593 (1967), point 40.
J. H. Hildebrand and R. L. Scott, Regular Solutions, Prentice-Hall, Englewood Cliffs, N.J. (1962), pp. 3–6.
J. H. Hildebrand, J. M. Prausnitz, and R. L. Scott, Regular and Related Solutions, Van Nostrand Reinhold, New York (1970), pp. 3–6.
J. A. Gerster, in: Perry’s Chemical Engineers’ Handbook, 4th ed., McGraw-Hill, New York (1963), p. 13–7.
R. E. Treybal, Liquid Extraction, McGraw-Hill, New York (1951), pp. 52–53.
L. N. Canjar, H. B. Ford, and R. T. Sebulsky, Petr. Ref, 36 (9): 291 (1957).
I. Prigogine and R. Defay, Chemical Thermodynamics, translated by D. H. Everett with revisions, J. Wiley and Sons, New York (1954), pp. 335–339, 391–392.
E. W. Slocum and B. F. Dodge, AIChE J., 10 (3): 364 (1964).
G. M. Wilson, in: Advances in Cryogenic Engineering, Vol. 9, Springer Science+Business Media New York (1964), p. 168.
G. M. Wilson, in: Advances in Cryogenic Engineering, Vol. 11, Springer Science+Business Media New York (1966), p. 392.
G. M. Wilson, paper 15e presented at 65th National AIChE Meeting, Cleveland, Ohio, May 4–7, 1969. Points 9b, 19, 28, 30, 32, 37 are accurately fitted by (9).
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Latimer, R.E. (1972). Liquid-Phase Activity Coefficients at 15 to 273°K. In: Timmerhaus, K.D. (eds) Advances in Cryogenic Engineering. Advances in Cryogenic Engineering, vol 17. Springer, Boston, MA. https://doi.org/10.1007/978-1-4684-7826-6_32
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