Abstract
The optimization of the catalytic performance of porous silicon enzyme microreactors with respect to the reactor geometry is reported. The microreactors were fabricated in p-type silicon with anisotropic KOH-etching. To increase the effective area the silicon was made porous by anodisation in a HF-ethanol solution. The performance of the different reactors was evaluated by coupling glucose oxidase onto the porous matrix and measuring the catalytic turn-over rate.
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