content material: the answer thought modeling of fuel adsorption on zeolites / Arthur W. Woltman and William H. Hartwig --
Mathematical modeling of adsorption in multicomponent structures / Alexander P. Mathews and Walter J. Weber, Jr. --
examine of combination 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 combos with pelleted zeolite beds / Richard T. Maurer --
impression of presorbed water at the sorption of nitrogen by way 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 influence of oxygen of photoluminescence and resonance strength move in copper (I) Y zeolite / D.H. Strome and okay. 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 trade of zeolite NaA / Elliot P. Hertzenberg and Howard S. Sherry --
Liquid section 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 by way of heatless adsorption / M.D. Whitley and C.E. Hamrin, Jr. / a brand new strategy for adsorption separation of fuel streams --
George E. Keller, II and Russell L. Jones.
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Extra resources for Adsorption and Ion Exchange with Synthetic Zeolites. Principles and Practice
In this paper we report experimental and theoretical results on the sorption of methane and krypton on 5A zeolite. The sorption of methane i n the 5A cavity i s reported to be nonlocalized (9), whereas that of krypton i s localized at a cavity site and window site (10). The multicomponent form of the isotherm of Schirmer et a l . i s used to interpret the experimental data and to predict mixture equilibria at other concentrations. Theory In the model of Schirmer et a l . ) for sorption i n zeolites, the canonical partition function q(i) i s expressed as g(i)X assuming the residual contributions of moments, rotations and internal motions are unchanged in moving from the gas to the sorbed phase.
T - E. T - E. ; ACS Symposium Series; American Chemical Society: Washington, DC, 1980. 3. LOUGHLIN AND ROBERTS CH k 57 & Kr Mixture Equilibria The index m, representing the maximum sorption i n the cavity, may be derived from considerations of the z e o l i t i c cavity volume and molar volume of the sorbate, as ι < ν/β. However Schirmer et a l . ) state that a maximum of 6 terms has been used i n their work. The extension of this model to a multicomponent sorbate is straightforward, and presented elsewhere by the authors (8K The binary isotherm equation i s η m Ρ /Ρ Λ , Λ S/Γ - Ε 4 Α ΟχΙ / Β o j _ _£ £-]} Σ Σ ΐ ί - ^ Γ (-fjf-y expUD RT j=o i=o ο ο N A / C / Ρ Γ 1 .
Eng. , 1964, SA3, 79. 23. Hiester, Ν. ; Chem. Eng. , 1952, 48, 505. 24. Keinath, T. ; Weber, W. ; "A Mathematical Model for Prediction of Concentration-Time Profiles for Design of Fluid-Bed Adsorbers," Tech. , Res. Project No. WP00706, Fed. Water Poll. S. Dept. of Interior, April 1968. 25. ; Smith, J. ; AIChE J . , 1974, 20, 88. 26. Toor, H. ; AIChE J . , 1957, 3, 198. 27. Fitts, D. ; "Nonequilibrium Thermodynamics," McGraw Hill, New York, 1962. RECEIVED May 13, 1980. ; ACS Symposium Series; American Chemical Society: Washington, DC, 1980.