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content material: the answer concept modeling of fuel adsorption on zeolites / Arthur W. Woltman and William H. Hartwig --
Mathematical modeling of adsorption in multicomponent platforms / Alexander P. Mathews and Walter J. Weber, Jr. --
examine of mix equilibria of methane and krypton on 5A zeolite / K.F. Loughlin and G.D. Roberts --
obvious floor diffusion results for carbon dioxide/air and carbon dioxide/nitrogen combinations with pelleted zeolite beds / Richard T. Maurer --
effect of presorbed water at the sorption of nitrogen by means of zeolites at ambient temperatures / Donald Peterson --
Selective sorption homes of zeolites / R.M. Dessau --
4 crystal buildings of BaxNa₁₂₂x-A (1[less than or equivalent to] x [less than or equivalent to] 6) in terms of the instability of barium-exchanged zeolite A towards dehydration / Yang Kim, V. Subramanian, Roger L. Firor, and Karl Seff --
The impression of oxygen of photoluminescence and resonance power move in copper (I) Y zeolite / D.H. Strome and ok. Klier --
coaching of copper(II)-exchanged Y zeolites from sodium and ammonium Y zeolites / Richard G. Herman and John B. Bulko --
Lead and cadmium ion alternate of zeolite NaA / Elliot P. Hertzenberg and Howard S. Sherry --
Liquid part drying functions of zeolites / George W. younger, Joseph R. Kiovsky, and Pramod B. Koradia --
Separation of n-paraffins from wax distillate with supercritical fluids and molecular sieves / Paul Barton and David F. Hajnik --
Polybed pressure-swing adsorption hydrogen processing / R.T. Cassidy --
Separation of hydrogen sulfide-hydrogen combinations via heatless adsorption / M.D. Whitley and C.E. Hamrin, Jr. / a brand new approach for adsorption separation of gasoline streams --
George E. Keller, II and Russell L. Jones.

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Additional resources for Adsorption and Ion Exchange with Synthetic Zeolites. Principles and Practice

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It i s seen that most of the data points are well within a deviation of ±20%. The results for these diverse solute systems indicate that equation (14) i s suitable for correlating binary equilibrium data for use in multicomponent rate models. Estimation of Rate Parameter The rate parameters of importance i n the multicomponent rate model are the mass transfer coefficients and surface diffusion coefficients for each solute species. For accurate description of the multicomponent rate kinetics, i t i s necessary that accurate values are used for these parameters.

Statistical Thermodyna­ mics," London, England, Cambridge University Press, 1939. 11. Dubinin, Μ. , J. , 1967, 23, 487. 12. Harper, R. , Stifel G R. and Anderson R Β. , 1969, 47, 4661 13. Flock, J. W. and Lyon 1974, 19, 205. 14. , Hirata, M. , J . of Chem. and Eng. Data, 1975, 20, 195. 15. Barrer, R. M. and Stuart, W. , Proc. Roy. , London, 1959, 249A, 464. 16. Broussard, L. , J. Amer. Chem. , 1960, 82, 1041. 17. Barrer, R. M. and Gibbons, R. , Trans. , 1963, 59, 2569. 18. Breck, D. , 1974. RECEIVED April 24, 1980.

1954. 10. Fowler, M. A. and Guggenheim, Ε. , "Statistical Thermodyna­ mics," London, England, Cambridge University Press, 1939. 11. Dubinin, Μ. , J. , 1967, 23, 487. 12. Harper, R. , Stifel G R. and Anderson R Β. , 1969, 47, 4661 13. Flock, J. W. and Lyon 1974, 19, 205. 14. , Hirata, M. , J . of Chem. and Eng. Data, 1975, 20, 195. 15. Barrer, R. M. and Stuart, W. , Proc. Roy. , London, 1959, 249A, 464. 16. Broussard, L. , J. Amer. Chem. , 1960, 82, 1041. 17. Barrer, R. M. and Gibbons, R. , Trans.

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