Ind. Eng. Chem. Process Des. Dev. 1982, 21, 457-465 457 days this operating procedure has wide perspectives in industrial adsorption separation. If a complete mathematical model whose parameter values are obtained by a few experimental runs is available, it is possible to explore the whole range of operating conditions without restrictions and therefore to obtain a proper design. Acknowledgment from SISAS S.p.A. Nomenclature a = external particle surface/particle volume, l/cm c, = concentration in external liquid phase, mol/L ci = concentration in liquid phase into macroporosity (internal Deff = effective diffusion coefficient (eq E), cm2/s DL = axial diffusion coefficient, cm2/s fq = mathematical expression of adsorption isotherm k , = film mass transfer coefficient, cm/s ki = intraparticle mass transfer coefficient (into macroporosity), cm/s K = equilibrium constant of adsorption, L/mol K, K* = pseudolinear equilibrium constant of adsorption, defined by eq 10, 12, L/mol KL = global mass transfer coefficient, cm/s L = length of the column, cm N.C. = number of the components Pe = Peclet number (= 2uRp/D~.e,) R, = radius of spherical particle equivalent to the solid pellet, t = time, s tR = retention time of a component t (= L/u), s u = fluid velocity, cm/s u = interstitial fluid velocity, cm/s u j = effective velocity of component j (eq ll), cm/s z = axial length coordinate, cm Greek Symbols a, p = coefficients introduced in eq 21 The authors gratefully acknowledge financial support phase), mol/L cm L i t e r a t u r e Cited Broughton, D. B.; Neuzll, R. W.; Pharis, J. M.; Brearley, C. S. Chem. Eng. Prog. 1970. 66, 70. Butt, J. B. "Reaction Kinetics and Reactor Design"; Rentice-Hall: Engelwood Cllffs, NJ, 1960 p 274. De Rosset, A. J.; NeuzU, R. W.; Korous, D. J. Ind. Eng . Chem . Process Des. Dev. 1978, 15, 261. Garg, D. R.; Ruthven, D. M. Chem. Eng. Sci. 1974. 29, 571. Keulemans, A. I. M. "Qas Chromatography", 2nd ed.; Relnhold New York, Liapis, A. I.; Rlppin, D. W. T. Chem. €ng. Sci. 1977, 33, 593. Morbldelll. M.; Servida, A.; Can& S. submltted to Chem. Eng. Comp. 1982. Santacesarla, E.; MorbMelll, M.; Denise, P.; Mercenari, M.; C a d , S. Ind. Eng. Chem. Process Des. Dev. 1982a. Part 1 of thls series, published in this issue. Santacesaria, E.; Morbldelli, M.; Servlda, A.; Storti, G.; Car& S. Ind. Eng. Chem. Process Des. Dev. 1882b. Part 2 of this series, publlshed in thls Issue. Seko, M.; Mlyake, T.; Inada, K.