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. 2015 Feb 9;2(1):35-53.
doi: 10.3390/bioengineering2010035.

Microbial Community Shifts during Biogas Production from Biowaste and/or Propionate

Affiliations

Microbial Community Shifts during Biogas Production from Biowaste and/or Propionate

Chaoran Li et al. Bioengineering (Basel). .

Abstract

Propionate is the most delicate intermediate during anaerobic digestion as its degradation is thermodynamically unfavorable. To determine its maximum possible degradation rates during anaerobic digestion, a reactor was fed Monday to Friday with an organic loading rate (OLR) of 12/14 kg CODbiowaste·m-3·d-1 plus propionate up to a final OLR of 18 kg COD·m-3·d-1. No feed was supplied on weekends as it was the case in full-scale. To maintain permanently high propionate oxidizing activity (POA), a basic OLR of 3 kg CODpropionate·m-3·d-1 all week + 11 kg CODbiowaste·m-3·d-1 from Monday to Friday was supplied. Finally a reactor was operated with an OLR of 12 kg CODbiowaste·m-3·d-1 from Monday to Friday and 5 kg CODpropionate·m-3·d-1 from Friday night to Monday morning to maintain a constant gas production for permanent operation of a gas engine. The propionate degradation rates (PDRs) were determined for biowaste + propionate feeding. Decreasing PDRs during starvation were analyzed. The POA was higher after propionate supply than after biowaste feeding and decreased faster during starvation of a propionate-fed rather than a biowaste-fed inoculum. Shifts of the propionate-oxidizing and methanogenic community were determined.

Keywords: anaerobic co-digestion; biowaste; community shifts; methanogenic community; propionate; propionate-oxidizing bacteria (POB).

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Conflict of interest statement

The authors declare no conflict of interest.

Figures

Figure 1
Figure 1
Scheme of reactors.
Figure 2
Figure 2
Biogas production and fatty acid levels in a 10 L biowaste reactor 1 after start at an OLR of 12 kg CODbiowaste·m−3·d−1 (a) and in reactor 2 for increasing organic loading rates up to 18 kg COD·m−3·d−1, maintained by 12 kg (day 1–55) or 14 kg (new batch biowaste from day 55 onwards) CODbiowaste·m−3·d−1 plus respective amounts of propionate (b). No feeding between days 75–85 due to maintenance work.
Figure 3
Figure 3
Biogas production (a) and fatty acid levels (b) in a 10 L biowaste digester (reactor 3) fed constantly with propionate (2.68 mM, 80 mL·d−1) at an OLR of 3 kg COD·m3·d1 and additionally with biowaste from Monday to Friday (1 L·d−1) to reach an OLR of 14 kg COD·m3·d1.
Figure 4
Figure 4
Periodic feeding of biowaste (BW, 1 L·d−1) or propionate (Prop, 2.68 M, 120 mL·d−1) to maintain an almost constant gas production in the 10 L biowaste reactor 4 over weekends, when no biowaste was available. No fatty acids were detected at any time.
Figure 5
Figure 5
Propionate degradation rates (a) and degradation activity immediately following starvation in effluent of reactor 4 or after 1–5 days, after biowaste (b) or propionate feeding (c).
Figure 6
Figure 6
Total Bacteria and Archaea (a), propionate-oxidizing bacteria (POB; b, c), and methanogenic archaea (d) in reactor 2, during feeding of biowaste at an OLR of 12 (day 1–55) or 14 (day 55 onwards) kg CODbiowaste·m−3·d−1 and propionate up to 4 kg CODpropionate·m−3·d−1. For sample preparation see Section 2.4.

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References

    1. McMahon K., Theng D., Stams A., Mackie R., Raskin L. Microbial population dynamics during start up and overload conditions of anaerobic digesters treating municipal solid waste and sewage sludge. Biotechnol. Bioeng. 2004;87:823–834. doi: 10.1002/bit.20192. - DOI - PubMed
    1. Gallert C., Henning A., Winter J. Scale-up of anaerobic digestion of the organic fraction from domestic wastes. Water Res. 2003;37:1433–1441. doi: 10.1016/S0043-1354(02)00537-7. - DOI - PubMed
    1. Gallert C., Winter J. Bacterial metabolism in wastewater treatment systems. In: Jördening H.J., Winter J., editors. Environmental Biotechnology—Concepts and Applications. Wiley-VCH; Weinheim, Germany: 2005. pp. 1–48.
    1. Gallert C., Winter J. Propionic acid accumulation and degradation during start-up of anaerobic biowaste digestion. Bioresour. Technol. 2008;99:170–178. doi: 10.1016/j.biortech.2006.11.014. - DOI - PubMed
    1. Li J., Ban Q., Zhang L., Jha A.K. Syntrophic propionate degradation in anaerobic digestion: A review. Int. J. Agric. Biol. 2012;14:843–850.

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