ISSN:
1588-2837
Keywords:
Partial oxidation
;
hydrocarbons
;
catalyst circulation
;
multiplicity
Source:
Springer Online Journal Archives 1860-2000
Topics:
Chemistry and Pharmacology
Notes:
Abstract A mathematical modeling of a dual-reactor system based on a simple kinetic scheme with two types of sites (accounting for deep and partial oxidation) has been performed. It has been shown that it is possible to regulate the state of a catalyst in the reaction zone by varying the rate of the catalyst circulation between the reactors, thus, significantly increasing the reaction selectivity. A region of multiplicity of the process stationary regimes has been found. This region appeared to become smaller with the increase of the catalyst circulation rate.
Type of Medium:
Electronic Resource
URL:
http://dx.doi.org/10.1007/BF02475850
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