Biofiltration is
a simple and low-cost method for the cleanup of
contaminated water. However, the reduced availability of dissolved
chemicals to surface-attached degrader bacteria may limit its efficient
use at certain hydraulic loadings. When a direct current (DC) electric
field is applied to an immersed packed bed, it invokes electrokinetic
processes, such as electroosmotic water flow (EOF). EOF is a surface-charge-induced
plug-flow-shaped movement of pore fluids. It acts at a nanometer distance
above surfaces and allows the change of microscale pressure-driven
flow profiles and, hence, the availability of dissolved contaminants
to microbial degraders. In laboratory percolation columns, we assessed
the effects of a weak DC electric field (E = 0.5
V·cm–1) on the biodegradation of waterborne
naphthalene (NAH) by surface-attached Pseudomonas fluorescens LP6a. To vary NAH bioavailability, we used different NAH concentrations
(C
0 = 2.7, 5.1, or 7.8 × 10–5 mol·L–1) and Darcy velocities typical for
biofiltration (
U̅
= 0.2–1.2 × 10–4 m·s–1). In DC-free controls, we observed
higher specific degradation rates (q
c)
at higher NAH concentrations. The q
c depended
on
U̅
, suggesting bioavailability restrictions
depending on the hydraulic residence times. DC fields consistently
increased q
c and resulted in linearly
increasing benefits up to 55% with rising hydraulic loadings relative
to controls. We explain these biodegradation benefits by EOF-altered
microscale flow profiles allowing for better NAH provision to bacteria
attached to the collectors even though the EOF was calculated to be
100–800 times smaller than bulk water flow. Our data suggest
that electrokinetic approaches may give rise to future technical applications
that allow regulating biodegradation, for example, in response to
fluctuating hydraulic loadings.