Biofuel cells typically yield lower power and are more difficult to fabricate than conventional fuel cells using inorganic catalysts. This work presents a glucose/O2 microfluidic biofuel cell (MBFC) featuring pyrolyzed photoresist film (PPF) electrodes made on silicon wafers using a rapid thermal process, and subsequently encapsulated by rapid prototyping techniques into a double-Y-shaped microchannel made entirely of plastic. A ferrocenium-based polyethyleneimine polymer linked to glucose oxidase (GOx/Fc-C6-LPEI) was used in the anode, while the cathode contained a mixture of laccase, anthracene-modified multi-walled carbon nanotubes, and tetrabutylammonium bromide-modified Nafion (MWCNTs/laccase/TBAB-Nafion). The cell performance was studied under different flow-rates, obtaining a maximum open circuit voltage of 0.54 ± 0.04 V and a maximum current density of 290 ± 28 μA cm(-2) at room temperature under a flow rate of 70 μL min(-1) representing a maximum power density of 64 ± 5 μW cm(-2). Although there is room for improvement, this is the best performance reported to date for a bioelectrode-based microfluidic enzymatic biofuel cell, and its materials and fabrication are amenable to mass production.
In this paper we describe the design, fabrication, and
characterization
of cylindrical gold micropillar array electrodes. Micropillar array
electrodes bring about several advantages compared to planar electrodes
and microelectrode arrays, as they provide a much larger surface area
than the latter devices. Micropillar array electrodes are closely
related to porous electrodes, as suggested by the recent literature
and as our experimental results show. We fabricated a number of different
gold micropillar array structures using standard microfabrication
techniques, particularly DRIE plasma etching, thermal oxidations,
and gold metallization by dc sputtering. Experimental results were
compared with simulations, and very good agreement was found. This
served both to validate the diffusion domain approximation for these
particular devices and also to deepen our understanding on the modes
of mass transport controlling the current response of these devices.
We found that planar diffusion dominates the response of these devices
and that thin layer diffusion effects play a crucial role and are
responsible for both displacing the position of the peaks and narrowing
the peak-to-peak separation in cyclic voltammograms. These effects
arise only as a result of the surface topology and should not be mistaken
by catalytic effects.
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