Abstract:
:For the application of immobilized enzymes, fixed bed reactors are used almost exclusively. Fixed bed reactors have specific disadvantages, especially for processes with a deactivating catalyst. Therefore, we have studied a novel reactor type with continuous transport of the immobilized biocatalyst. Flow of biocatalyst is countercurrent to the substrate solution. Because of a stagewise reactor design, back-mixing of biocatalyst is very limited and transport is nearly plug flow. The reactor operates at a constant flow rate and conversion, due to constant holdup of catalytic activity. The reactor performance is compared with a configuration of fixed bed reactors. For reactions in the first-order regime, enzyme requirements in this new reactor are slightly less than for fixed bed processes. The multistage fluidized bed appears to be an attractive reactor design to use biocatalyst to a low residual activity. However, nonuniformity of the particles might affect plug flow transport of the biocatalyst. A laboratory scale reactor and experiments are described in Part II(1) of this series. Hydrodynamic design aspects of a multistage fluidized bed are discussed in more detail in Part III.(2).
journal_name
Biotechnol Bioengjournal_title
Biotechnology and bioengineeringauthors
Vos HJ,Groen DJ,Potters JJ,Luyben KCdoi
10.1002/bit.260360407subject
Has Abstractpub_date
1990-08-05 00:00:00pages
367-76issue
4eissn
0006-3592issn
1097-0290journal_volume
36pub_type
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