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Modelling of affinity separation by batch and fixed bed adsorption – a comparative study
Author(s) -
Sridhar P.
Publication year - 1996
Publication title -
chemical engineering and technology
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.403
H-Index - 81
eISSN - 1521-4125
pISSN - 0930-7516
DOI - 10.1002/ceat.270190409
Subject(s) - adsorption , mass transfer , orthogonal collocation , diffusion , chromatography , particle size , chemistry , kinetics , batch processing , particle (ecology) , chemical engineering , thermodynamics , materials science , mathematics , collocation method , computer science , physics , engineering , differential equation , mathematical analysis , ordinary differential equation , oceanography , quantum mechanics , geology , programming language
Affinity separation can be achieved by batch and fixed bed modes. Mathematical models including film mass transfer, intraparticle diffusion, and reversible reaction are formulated for both fixed bed and batch adsorption processes. Orthogonal collocation method is used to numerically evaluate the performance of batch and fixed bed adsorption. The efficiencies are evaluated in terms of both the solute recovery and adsorbent utilization. The effect of the following parameters is simulated for the comparison purpose: solute concentration, reaction kinetics, ligand content, and particle size. Fixed bed mode is found to be efficient.