초록
<P><B>Abstract</B></P> <P>An anaerobic sequencing batch biofilm reactor (AnSBBR) with recirculation of the liquid phase (at 30？°C with 3.5？L of working volume and treating 1.5？L per cycle) treating pure glycerin-based wastewater was applied to biohydrogen production. The applied volumetric organic load (AVOL) ranged from 7.7 to 17.1？kgCOD？m<SUP>−3</SUP>？d<SUP>−1</SUP>, combining different influent concentrations (3000, 4000 and 5000？mgCOD？L<SUP>−1</SUP>) and cycle lengths (4 and 3？h). The feed strategy used was to maintain the feeding time equal to half of the cycle time. The increase in the influent concentration and the decrease in cycle length improved the molar yield and molar productivity of hydrogen. The highest productivity (100.8？molH<SUB>2</SUB>？m<SUP>−3</SUP>？d<SUP>−1</SUP>) and highest yield of hydrogen per load removed (20.0？molH<SUB>2</SUB>？kgCOD<SUP>−1</SUP>) were reached when the reactor operated with an AVOL of 17.1？kgCOD？m<SUP>−3</SUP>？d<SUP>−1</SUP>, with 68% of H<SUB>2</SUB> and only 3% of CH<SUB>4</SUB> in its biogas. It was also found that pretreatment of the sludge/inoculum does not influence the productivity/yield of the process and the use of crude industrial glycerin-based wastewater in relation to the pure glycerol-based wastewater substantially decreased the production and composition of the hydrogen produced.</P> <P><B>Highlights</B></P> <P> <UL> <LI> An AnSBBR was applied for biohydrogen production by treating glycerin wastewater. </LI> <LI> The biohydrogen production was stable, but inhibition of methanogenesis was not achieved. </LI> <LI> The higher the influent concentration, the higher the hydrogen productivity. </LI> <LI> The shorter the cycle, the higher the hydrogen productivity. </LI> <LI> The process proposed is feasible for biohydrogen production. </LI> </UL> </P>