Enzyme reactors were fabricated on silicon wafers using microstructuri
ng technologies. The reactors were made of several parallel vertically
-cut flow channels. The reactor structures occupied a wafer area of 3
15 mm. Reactors with two different channel densities were fabricated
: 10 channels/mm, 165 mu m deep; and 25 channels/mm, 235 mu m deep. Gl
ucose oxidase was immobilised on the reactors and their corresponding
enzyme activities were monitored by a colourimetric assay. It was show
n that a reactor surface area increase of 3 times gave rise to a propo
rtional enzyme activity increase in the reactor. The maximum glucose t
urnover rate for the reactor with 25 channels/mm was approximately 35
nmol/minute and the corresponding apparent K-m was approximately 17 mM
. A wafer integrated enzyme reactor was also operated in a microdialys
is-based system for continuous glucose monitoring, showing a linear re
sponse up to 4 mM glucose.