The hydrodynamic resistance in a biocatalyst particle fixed bed reacto
r was studied. The biocatalyst used was immobilized glucose isomerase
supported by an organic carrier composed of cross-linked proteins. The
bed structural deterioration caused by compression-enhanced particle
fragmentation and washing-out was considered. The resistance functions
(friction factor vs. Re) for four different cases of polydisperse mat
erial with increasing spread of the size distribution, corresponding t
o different extents of particle destruction, were evaluated. The exper
iments were repeated with three different values of the bed compressio
n, corresponding to different sample positions in the large-scale isom
erization column. The relationships obtained exhibited slopes slightly
greater than those predicted theoretically for stable packings. This
effect can be explained by the increased irregularity of voids due to
bed degradation, accompanied by the formation of hollow spaces and sud
den changes in the cross-section of the channels. A semiempirical corr
elation recommended by Reichelt was found to represent the experimenta
l data well for the practically important region of Re > 0.5.