AI summary

78% confidence

This study demonstrates that H-type MFCs fed with anaerobic digestate can simultaneously generate electricity and remove nitrogen through the spontaneous establishment of electroactive and anammox bacteria. Two reactors—one with a sterile anode (MFC-U) and one pre-colonized with Geobacter sulfurreducens (MFC-C)—achieved comparable power densities (172.2 and 240 mW/m² respectively) and removed 32–40% of total Kjeldahl nitrogen (TKN) while reducing COD by 60–68%. Molecular analysis confirmed anammox bacteria colonization in the anode biofilm. The work suggests MFCs can recover slow-growing anammox organisms from natural sources without external enrichment, though the nitrogen removal mechanism remains incompletely characterized.

Key insights

  • Performance Unconditioned digestate-derived biofilms achieved 172.2 mW/m² power density, only 28% lower than G. sulfurreducens-preconditioned anodes at 240 mW/m², despite a 3-week delayed start-up.

    So what. Preconditioning with pure cultures may not be necessary for digestate-fed MFCs; natural inoculation can achieve comparable performance if start-up delay is acceptable.

  • Mechanism Coulombic efficiency was low (15.6–19.6%) despite zero methane production and negligible nitrate/nitrite accumulation, suggesting anaerobic ammonia oxidation rather than direct ammonia-to-electricity conversion.

    So what. Low CE in digestate-fed MFCs should not be interpreted as poor performance; it reflects substrate partitioning to anammox and other non-electrogenic pathways, not methanogenesis or diffusion losses.

  • Mechanism Anammox bacteria were enriched in the anode biofilm (detected by 16S rRNA and nitrite reductase gene PCR) despite anaerobic conditions and no external enrichment culture, indicating the MFC anode selects for these slow-growing organisms.

    So what. MFC anodes may serve as passive enrichment reactors for anammox; test whether anode potential or biofilm age accelerates anammox establishment compared to conventional enrichment.

  • Mechanism Biofilm thickness was similar (66–141 μm) in both reactors, but MFC-C showed uniform multilayered structure while MFC-U showed composite morphology with surface-localized bacteria and entrapped sediments.

    So what. Biofilm architecture differs by inoculum source; digestate-derived biofilms may require longer maturation or different anode materials to achieve the ordered structure of pure-culture biofilms.

  • Performance Live bacteria comprised ~30% of biofilm depth in both reactors, concentrated in the outer 0–3 μm layer, yet current generation remained comparable to prior studies using carbon cloth anodes.

    So what. Dead cell layers do not significantly impede electron transfer in digestate-fed MFCs; focus optimization on outer biofilm activity rather than bulk viability.

Opportunity areas6

Specific gaps in this paper, with an experiment that would close each.

  • High No measurement of anode or cathode potential (vs. Ag/AgCl or SHE); operating window for anammox enrichment and nitrogen removal is unknown.

    Section 2.2 states 'fixed external resistance, Rext, of 180 Ω' but does not report actual anode or cathode potentials. Polarization curves (Figure 3) show voltage and current but not electrode potentials. Anammox bacteria have known redox preferences; without potential data, the electrochemical conditions driving their enrichment cannot be replicated or optimized.

    Try. Measure anode and cathode potential (vs. Ag/AgCl) throughout batch cycles; vary anode potential (−0.2 to +0.2 V) and quantify anammox 16S rRNA gene abundance and nitrogen removal rate.

  • High No dissolved oxygen (DO) measurement in the anode chamber during operation; anaerobic conditions assumed but not verified.

    Section 2.4 lists DO measurement capability ('dissolved oxygen was measured with a 913 OXY oximeter') but Section 3.3 only states 'dissolved oxygen in the anodic chambers was always lower than 0.05 mg/L' without time-series data or sampling frequency. Anammox requires strict anaerobiosis; DO leakage would shift nitrogen removal toward nitrification-denitrification.

    Try. Log DO continuously in anode chamber; correlate with anammox gene abundance and nitrite/nitrate accumulation; test membrane integrity and N2 flushing frequency.

  • High No measurement of nitrite (NO2−) or nitrate (NO3−) accumulation in the anode chamber; only stated as 'negligible' at cycle end.

    Section 3.3 states 'nitrates and nitrites at the end of each cycle were negligible in the anodic and cathodic chambers' but provides no time-series data, detection limits, or quantitative values. Anammox consumes NO2− and produces N2; transient NO2− accumulation would confirm anammox activity but is not tracked.

    Try. Measure NO2− and NO3− daily by ion chromatography (method already available, Section 2.4); plot against TKN removal and anammox gene expression; test whether NO2− limitation constrains nitrogen removal.

  • Medium No variation in C/N ratio or HRT; single digestate dilution (1:10) and weekly feeding tested.

    Section 2.1 and 2.2 describe a fixed feed composition (1:10 digestate dilution, weekly replacement of 150 mL of 200 mL anode volume, ~7-day HRT). No exploration of how C/N ratio or residence time affects anammox enrichment or nitrogen removal efficiency. Anammox typically requires low C/N and long HRT.

    Try. Test digestate dilutions (1:5, 1:10, 1:20) and feeding intervals (3, 7, 14 days); measure TKN removal, anammox gene copy number, and power output.

  • Medium No measurement of N2O or N2 gas production; nitrogen balance incomplete.

    Section 3.3 states 'we did not detect CH4 production' but does not report N2O or N2 measurement. Anammox produces N2; denitrification can produce N2O. Without gas chromatography or isotope tracing, the fate of 32–40% removed TKN is unknown—it could be biomass incorporation, N2 loss, or N2O accumulation.

    Try. Measure headspace N2O by GC-ECD and N2 by GC-TCD or isotope-labeled 15N tracing; quantify nitrogen balance and confirm anammox stoichiometry (NH4+ + NO2− → N2 + 2H2O).

  • Medium No catholyte pH control or monitoring; neutral pH assumed but not reported.

    Section 2.2 states cathode filled with 'potassium phosphate buffer (100 mM pH 7.5)' but no pH time-series or post-operation pH reported. Cathode pH can drift due to proton consumption during reduction; anammox in cathode chamber (if any) would be pH-sensitive.

    Try. Monitor cathode pH continuously; test pH range (6.5–8.5) and measure anammox activity and nitrogen removal in cathode chamber if applicable.

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What they did

System
MFC

What worked

Power density240mW/m²best of 4
Current density1.30A/m²best of 2
Coulombic efficiency19.6%best of 2
COD removal68.0%best of 2

Abstract

Microbial Fuel cells (MFCs) have been proposed for nutrient removal and energy recovery from different wastes. In this study the anaerobic digestate was used to feed H-type MFC reactors, one with a graphite anode preconditioned with Geobacter sulfurreducens and the other with an unconditioned graphite anode. The data demonstrate that the digestate acts as a carbon source, and even in the absence of anode preconditioning, electroactive bacteria colonise the anodic chamber, producing a maximum power density of 172.2 mW/m². The carbon content was also reduced by up to 60%, while anaerobic ammonium oxidation (anammox) bacteria, which were found in the anodic compartment of the reactors, contributed to nitrogen removal from the digestate. Overall, these results demonstrate that MFCs can be used to recover anammox bacteria from natural sources, and it may represent a promising bioremediation unit in anaerobic digestor plants for the simultaneous nitrogen removal and electricity generation using digestate as substrate.

Keywords

DigestateMicrobial fuel cellAnammoxGeobacterGeobacter sulfurreducensAnodePulp and paper industryChemistryAnaerobic digestionEnergy sourceAnaerobic bacteriaEnvironmental chemistryEnvironmental scienceNitrogenBiofilmBacteriaCoalMethaneDenitrificationBiologyElectrodeOrganic chemistry

Identifiers

Journal
BioMed Research International
Year
2015
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