(507c) Breakthrough Curves for Solid-Acid Catalyzed Liquid-Phase Alkylation Reactions | AIChE

(507c) Breakthrough Curves for Solid-Acid Catalyzed Liquid-Phase Alkylation Reactions

Authors 

Nayak, S. - Presenter, Washington University in St Louis
Al-Dahhan, M. - Presenter, Washington University in St Louis
Dudukovic, M. - Presenter, Washington University in St Louis
Sarsani, V. - Presenter, University of Kansas
Subramaniam, B. - Presenter, Center for Environmentally Beneficial Catalysis, University of Kansas


The use of environmentally benign solid acid catalysts for liquid phase isoparaffin/olefin alkylation has been investigated since early 1970's. The major drawback of this process is rapid deactivation of solid-acid catalysts because of fouling by hydro-carbonaceous deposits. Recent study has shown in carbon-dioxide expanded solvent under high pressure and /or temperature the pore cleaning may be achieved (Lyon et al 2004). So it is important to know the adsorption, desorption and reaction parameters on solid-acid catalyst to enhance the product selectivity and decrease the rate of deactivation. By studying the breakthrough curves in packed-bed reactor one can determine this parameters. Two methods can be used to determine these parameters; model dependent numerical algorithm and model independent method of moments. In current work both this methods are used for solid-acid catalyzed alkylation reactions. It is found that Method of Moments provides approximates expression for the break through curve that are useful for scale-up and reactor design.

Reference Lyon. C., Sarsani. V., Subramaniam B ?1-Butene + Isobutane Reactions on Solid Acid Catalysts in Dense CO2-Based Reaction Media: Experiments and Modeling? Ind. Eng. Chem. Res. 2004, 4, 480-481.