An autotrophic biological process for the treatment of nitrate-contaminated
drinking water was studied in the laboratory, with the objective of develo
ping a continuous system which would be simple, stable and amenable to upsc
aling. Hydrogen generated by electrolysis of the water to be treated was th
e source of energy for denitrifying microorganisms. Two main process config
urations were compared: (1) a single reactor where both the generation of h
ydrogen and denitrification took place. and (2) a two-reactor system where
water was first enriched with hydrogen in an electrolysis cell prior to ent
ering a packed-bed bioreactor. The reactors were operated in a continuous m
ode and granulated activated carbon served as physical support for the biom
ass. Although the highest rates of denitrification (0.45 kgN m(-3) d(-1)) a
nd the shortest residence times (removal of 18 mg N l(-1) in 17 min) were o
btained in the single-reactor system, the two-reactor system was more stabl
e and more suitable for upscaling.