content material: the answer conception 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. --
learn 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 combos 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 houses 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 strength move in copper (I) Y zeolite / D.H. Strome and ok. Klier --
education 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 purposes 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 through heatless adsorption / M.D. Whitley and C.E. Hamrin, Jr. / a brand new approach for adsorption separation of fuel 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
Chambers Ε and C are connected by a second path containing an impeller pump, which i s magnetically s t i r r e d , and the Barocel pressure transducer has been removed. 1 mm, i s used to read a manometer for pressure measurement. The remaining equipment i s the same as reported previously ( l l ) . 36 kPa and the gas phase was continuously circulated between chambers Ε and C during runs to ensure uniformity of composition. The pressure was recorded using the manometer i n chamber A, opened to chamber C; to ensure uniformity of gas phase composition, the mercury reservoir R was period i c a l l y raised and lowered, exchanging the gas i n the top of chamber A with that i n chamber C.
The experimental data shown are independent of the order of contacting, demonstrating the consistency of the data. The range of sorbate coverage i s from 15$ at the highest temperature (271K) to k0% at the lowest temperature (238K). For this system saturation coverage i s 12 molecules/cavity for either component. At 271 and 255K the t o t a l amount adsorbed increases continuously with increasing mole fraction of methane, whereas at 238K the t o t a l amount adsorbed passes through a maximum at 60% methane i n the adsorbed phase.
MATHEWS AND WEBER Mathematical Modeling 29 Equation (3) allows the use of experimental equilibrium data i n multicomponent rate models. The transport of the adsorbed species into spherical parti cles i s represented by the unsteady state diffusion equation as follows: 8 «t \ "k * 6r And, H j- + ^ k = 1, Ν (5) 2 the material balance for the reactor i s : dc, v d F dq, = - w d T ' k Dfc i s the surface diffusion coefficient for each solute, V i s the volume of f l u i d i n the reactor, and W the weight of adsorbent in the reactor.