Biofilm photobioreactors for the treatment of industrial wastewaters.
A flat plate and a tubular packed-bed photobioreactor with an algal-bacterial biofilm attached onto Poraver beads carriers, a flat plate and a tubular photobioreactor with the biofilm attached onto the reactor walls, and an algal-turf reactor were compared in terms of BOD removal efficiencies, elimination capacities, and stability. A control column photobioreactor with suspended algal-bacterial biomass was also tested to compare the performance of biofilm photobioreactors with conventional algal-based processes. When the algal-bacterial biomass was immobilized onto Poraver the process never reached a steady state due to a poor homogenization in the bioreactor. When the biofilm was formed onto the reactor wall (or reactor base) the process was stable. A maximum degradation rate of 295mg BODl(-1)h(-1) was achieved in the algal-turf reactor although control experiments performed in the dark showed atmospheric O2 diffusion represented 55% of the oxygenation capacity in this system. BOD removal rates of 108, and 92mg BODl(-1)h(-1) were achieved in the tubular and flat plate biofilm reactors, respectively, compared to 77mg BODl(-1)h(-1) in the control suspended bioreactor. In addition, all biofilm photobioreactors produced an easily settleable biomass. Evidence was found that biomass attachment to the reactor's wall improved stability.
Muñoz
Raul
R
Department of Biotechnology, Center for Chemistry and Chemical Engineering, Lund University, Box 124, 22100 Lund, Sweden. mutora@iq.uva.es
Köllner
Claudia
C
Guieysse
Benoit
B
D018441:Biofilms; D019149:Bioreactors; D007220:Industrial Waste; D010777:Photochemistry; D012459:Salicylates / Q000302:isolation & purification; D014865:Waste Disposal, Fluid / Q000295:instrumentation* / Q000379:methods*
D007220:Industrial Waste; D012459:Salicylates