초록
<P><B>Abstract</B></P> <P>Most of the fermentative hydrogen production studies based on mixed cultures have shown enrichment of the microbial community by means of a heat treatment. This heat treatment enrichment strategy selects for <I>Clostridum</I> spp., an efficient hydrogen producer; however, other bacteria that may contribute to the systems performance could be excluded. Another enrichment strategy based on high dilution rates selects different taxonomic groups, which may affect hydrogen production and the system stability. In this work, two enrichment strategies were evaluated, heat shock and cell wash-out, for hydrogen production and the system stability in continuous stirred reactors. The enriched communities were then inoculated in packed bed reactors and operated up to 70 days. Both strategies selected hydrogen producing bacteria, mainly <I>Clostridium</I> spp. The highest hydrogen production rate (6.01 L H<SUB>2</SUB>/L-d), molar yield (1.29 mol H<SUB>2</SUB>/mol glucose<SUB>consumed</SUB>), and stability were achieved by the wash-out procedure; this high performance was attributed to facultative bacteria like <I>Lactobacillus</I> and <I>Lactococcus</I>. Furthermore, there was a transition within the community (along the operation time in the reactor with cell wash-out inoculum) and a selection for methanogenic activity (due to the long solids retention time).</P> <P><B>Highlights</B></P> <P> <UL> <LI> Heat shock and cell wash-out as strategies to enrich hydrogen producing bacteria. </LI> <LI> Enriched communities developed were inoculated in packed bed reactors. </LI> <LI> Cell wash-out prompted stability attributed to facultative bacteria. </LI> <LI> A transition from hydrogen producing community to a methanogenic one was observed. </LI> <LI> Strategies to get a stable hydrogen production in packed bed reactors are proposed. </LI> </UL> </P> <P><B>Graphical abstract</B></P> <P>[DISPLAY OMISSION]</P>