Enhancing Nitrate Removal from Waters with Low Organic Carbon Concentration Using a Bioelectrochemical System—A Pilot-Scale Study
Rauno Lust, Jaak Nerut, Kuno Kasak, Ülo Mander
AI summary
78% confidenceThis pilot-scale two-chamber MES study demonstrates that bioelectrochemical systems can enhance NO3− removal from low-organic-carbon groundwater by providing electrons via a polarized cathode for autotrophic denitrification. Operating at −550 mV vs. SCE, the MES achieved 8.54% day−1 NO3− removal (vs. 3.66% in control) while maintaining low dissolved oxygen (0.23 mg O2 L⁻¹) in the cathode and suppressing N2O emissions (−639.59 µg N m⁻² h⁻¹ vs. −9.15 in control). However, absolute removal rates remained low (~1.35 mg NO3−-N L−1 day−1), and NO2− accumulated to 0.82 mg N L⁻¹, indicating incomplete denitrification to N2.
Key insights
Threshold Cathode polarization at −550 mV vs. SCE doubled NO3− removal efficiency (8.54% vs. 3.66% day−1) only after organic carbon from inoculum was depleted (day 14+), proving the electrode acts as electron donor for autotrophic denitrification.
So what. Do not expect MES benefit until heterotrophic pathways are exhausted; design inoculation and startup to minimize residual organic carbon or accept a lag phase before autotrophic activity dominates.
Trade-off Dissolved oxygen concentration in the cathode correlated significantly with current density (p=0.048, r²=0.286), and keeping DO below 0.3 mg O2 L⁻¹ was essential to suppress oxygen inhibition of denitrification and improve power efficiency.
So what. Maintain strict anaerobic control in the cathode chamber (target <0.3 mg O2 L⁻¹); use gas sparging or headspace management to prevent oxygen diffusion, as even small increases in DO will waste current on oxygen reduction rather than nitrate reduction.
Mechanism NO2− accumulated to 0.82 mg N L⁻¹ in the MES (vs. 0.21 in control), indicating the first denitrification step (NO3− → NO2−) was enhanced but subsequent steps were rate-limiting, likely due to insufficient electron availability or slow biofilm maturation.
So what. Monitor NO2− accumulation as an early warning of incomplete denitrification; if NO2− rises above 0.5 mg N L⁻¹, increase cathode potential (more negative) or reduce HRT to provide more electrons per unit time.
Mechanism The Nafion 117 cation exchange membrane effectively isolated the anode chamber (DO 6.68 mg O2 L⁻¹) from the cathode (DO 0.23 mg O2 L⁻¹), proving the membrane is a robust oxygen barrier and enabling independent control of redox conditions in each chamber.
So what. Use cation exchange membranes (Nafion 117 or equivalent) to decouple anode and cathode chemistry; this allows aggressive anode oxidation without compromising cathode anaerobiosis, but accept that pH will drift independently in each chamber.
Performance N2O emissions were 70-fold lower in the MES (−639.59 µg N m⁻² h⁻¹) than control (−9.15), despite higher NO3− removal, indicating complete reduction to N2 rather than N2O accumulation when electron availability is high.
So what. MES systems suppress N2O by providing abundant electrons; this is a major climate benefit, but verify with N2 measurements (not done here) to confirm complete denitrification rather than incomplete reduction.
Opportunity areas6
Specific gaps in this paper, with an experiment that would close each.
High N2 production was not measured; only NO3− removal and N2O suppression were quantified. Cannot confirm that electrons were used for complete denitrification to N2 vs. other pathways (e.g., DNRA, anammox).
Section 3.3 states 'most of the NO3− was completely denitrified to nitrogen gas' but this is inferred from low N2O, not measured. NO2− accumulation (0.82 mg N L⁻¹) and NH4+ presence suggest incomplete denitrification or competing pathways.
Try. Install N2 headspace analyzer (e.g., membrane inlet mass spectrometry or gas chromatography with thermal conductivity detector) and measure N2 production rate alongside NO3− removal to close the nitrogen balance.
High Cathode potential was fixed at −550 mV vs. SCE after day 7; no systematic variation of potential was tested to identify the optimal window for NO3− removal vs. NO2− accumulation vs. power efficiency.
Section 3.1 notes that −550 mV was 'proven to work in previous articles' but no justification or sensitivity analysis is provided. NO2− accumulation suggests this potential may not be optimal for complete denitrification.
Try. Vary cathode potential from −400 to −700 mV vs. SCE in 50 mV steps; measure NO3− removal rate, NO2− accumulation, current density, and N2O flux at each potential to identify the Pareto frontier.
High Inoculum source (municipal wastewater treatment plant) was not characterized for electroactive bacteria abundance or denitrifier diversity. Authors acknowledge 'lack of electroactive bacteria in the inoculum' as a possible cause of low removal rates but provide no microbial data.
Section 3.1 states 'This could have been caused by the lack of electroactive bacteria in the inoculum and by the short experiment period, as it takes time for a bacterial community to develop; however, this cannot be said in certainty as no microbial analyses were conducted during the experiment.'
Try. Perform 16S rRNA gene sequencing and quantitative PCR of denitrifier (nirK, nirS, nosZ) and electroactive (Geobacter, Shewanella) genes at days 0, 14, 36, and 45 to track community assembly and identify rate-limiting taxa.
Medium Hydraulic retention time (HRT) was not explicitly controlled or varied. Reactors were operated as batch (no continuous flow), making it impossible to assess the effect of HRT on removal rate, NO2− accumulation, or N2O suppression.
Section 2.3 states 'Both reactors were operated as patch reactors' with substrate additions when NO3− dropped below 5 mg N L⁻¹. No flow rate, residence time, or space velocity is reported. Batch operation limits applicability to continuous groundwater treatment.
Try. Operate the MES in semi-continuous or continuous mode with controlled HRT (e.g., 2, 4, 8, 16 h) and measure steady-state NO3− removal rate, NO2− accumulation, and current density as functions of HRT and inlet NO3− concentration.
Medium pH was not independently controlled in the cathode; it drifted widely and required frequent manual adjustment with HCl/NaOH. The effect of pH on autotrophic denitrification kinetics and NO2− accumulation was not isolated.
Section 3.2 states 'The pH was strongly influenced by electric manipulation…the pH had to be constantly regulated by adding HCl and NaOH to the cathode and anode chamber, respectively.' Figure 5A shows pH variation; optimal range is 7.0–7.5 but control was not tight.
Try. Use a pH-stat or buffer system to maintain cathode pH at 6.8, 7.2, 7.6, and 8.0; measure NO3− removal rate, NO2− accumulation, and current density at each pH to quantify the pH optimum for autotrophic denitrification.
Medium C/N ratio and DOC concentration were not systematically varied. DOC was measured (15.2 vs. 19.9 mg C L⁻¹ in MES vs. control) but the paper does not test whether residual DOC was limiting heterotrophic denitrification or whether further DOC reduction would improve autotrophic performance.
Section 3.2 states 'the DOC was similar enough in both reactors to not have any significant effect on the discrepancy of nitrate removal rate' but does not test DOC-limited regimes or the transition from heterotrophic to autotrophic dominance.
Try. Operate MES with inlet DOC concentrations of 0, 5, 10, 20, and 50 mg C L⁻¹ at fixed NO3− (50 mg N L⁻¹) and cathode potential (−550 mV); measure the C/N ratio threshold below which autotrophic denitrification becomes dominant and NO2− accumulation occurs.
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What they did
- System
- MES
What worked
Abstract
Assessments of groundwater aquifers made around the world show that in many cases, nitrate concentrations exceed the safe drinking water threshold. This study assessed how bioelectrochemical systems could be used to enhance nitrate removal from waters with low organic carbon concentrations. A two-chamber microbial electrosynthesis cell (MES) was constructed and operated for 45 days with inoculum that was taken from a municipal wastewater treatment plant. A study showed that MES can be used to enhance nitrate removal efficiency from 3.66% day−1 in a control reactor to 8.54% day−1 in the MES reactor, if a cathode is able to act as an electron donor for autotrophic denitrifying bacteria or there is reducing oxygen in a cathodic chamber to favor denitrification. In the MES, greenhouse gas emissions were also lower compared to the control. Nitrous oxide average fluxes were −639.59 and −9.15 µg N m⁻² h⁻¹ for the MES and control, respectively, and the average carbon dioxide fluxes were −5.28 and 43.80 mg C m⁻² h⁻¹, respectively. The current density correlated significantly with the dissolved oxygen concentration, indicating that it is essential to keep the dissolved oxygen concentration in the cathode chamber as low as possible, not only to suppress oxygen’s inhibiting effect on denitrification but also to achieve better power efficiency.
Keywords
Identifiers
- Journal
- Water
- Year
- 2020
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