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SLU publication database (SLUpub) (stage, solr2:8983)

Abstract

Syngas biomethanation enables the use of recalcitrant biomass or waste for methane production. To reveal knowledge on the importance of nutrient medium supply rate (NMSR) and liquid recirculation regime, a thermophilic 5 L trickle-bed reactor was operated for 283 days. Efficient and stable operation with >99 % H-2 and CO conversion rates was achieved at a minimum NMSR of 14 mL/(L-pbvd) and 1 h gas retention time, yielding a maximum methane evolution rate (MER) of 4.3 L/(L-pbvd). Reduced intermittent liquid recirculation resulted in lowered MERs (max. 3.4 L/(L-pbvd)) with CO conversion more affected by low recirculation frequencies than H-2 conversion. The microbial analysis revealed a similar microbial community structure across all experimental phases, dominated by Methanothermobacter in both liquid and carrier biofilm. CO was likely converted to methane and acetate, with syntrophic acetate-oxidizing bacteria metabolizing acetate to H-2 and CO2, supporting efficient hydrogenotrophic methanogenesis.

Keywords

Biosyngas; Digestate; Hydraulic retention time; Trickling; Syntrophic acetate oxidation; Methanothermobacter

Published in

Bioresource technology reports
2025, volume: 32, article number: 102353
Publisher: ELSEVIER

SLU Authors

UKÄ Subject classification

Bioenergy

Publication identifier

  • DOI: https://doi.org/10.1016/j.biteb.2025.102353

Permanent link to this page (URI)

https://res.slu.se/id/publ/144562