Forschungsdaten – Titel und Zusammenfassungen von Publikationen, extrahierte Daten und Katalogeinträge – erscheinen in ihrer Originalsprache Englisch.

KI-Zusammenfassung

72 % Konfidenz

This study optimized a two-chamber MFC for simultaneous NH4+-N and TP removal using response surface methodology (RSM) with central composite design (CCD), varying HRT (12–24 h) and initial ammonia concentration (20–80 mg/L). Optimal conditions achieved 94.88% NH4+-N removal at HRT 24 h and 20 mg/L NH4+-N, and 59.39% TP removal at HRT 18 h and 45 mg/L NH4+-N. Microbial community analysis showed that optimization reduced species richness but enriched dominant nitrifying and heterotrophic taxa on the cathode, particularly Proteobacteria and Nitrospirae.

Zentrale Erkenntnisse

  • Zielkonflikt Initial ammonia concentration had greater impact on NH4+-N removal than HRT; coefficient of X2 (−11.253) was larger in magnitude than X1 (+11.183) in the linear model.

    Was heißt das. Prioritize controlling influent ammonia concentration over HRT adjustment when designing for ammonia removal; high ammonia (>40 mg/L FAN) inhibits nitrification and limits simultaneous nitritation/denitritation (SND).

  • Schwellenwert TP removal exhibited a peak response at intermediate conditions (HRT ~18 h, ammonia ~50 mg/L) rather than monotonic improvement, with removal rate first increasing then decreasing.

    Was heißt das. Avoid operating at extremes of HRT or ammonia concentration for TP removal; there is an optimal window around 18 h HRT and 45–50 mg/L NH4+-N where microbial community synergy is maximized.

  • Mechanismus Optimization reduced microbial species richness (Chao and ACE indices decreased in groups A and B vs. control C) but enriched dominant taxa, particularly Proteobacteria (39.68% → 44.41–47.02%) and Nitrospirae (2.34% → 4.97%).

    Was heißt das. Selective enrichment of nitrifiers and proteobacteria under optimized conditions indicates that moderate ammonia stress and longer HRT favor nitrification; monitor Nitrospirae abundance as a proxy for NOB activity and nitrification capacity.

  • Schwellenwert COD/N ratio of 5 (500 mg/L COD ÷ 100 mg/L N equivalent) achieved 87.2% COD removal and ~95% ammonia removal, but higher ammonia concentrations (>40 mg/L FAN) inhibited nitrification and limited SND.

    Was heißt das. Maintain ammonia concentration ≤40 mg/L and COD/N ratio near 5–7 to avoid inhibition of nitrifiers; higher ammonia acts as a stressor that selects against AOB/NOB even in the presence of sufficient organic carbon.

  • Zielkonflikt Longer HRT (24 h vs. 12 h) improved NH4+-N removal by increasing contact time between substrate and microorganisms, but excessive HRT reduced TP removal performance, indicating a trade-off between nitrogen and phosphorus removal kinetics.

    Was heißt das. Decouple optimization for NH4+-N (favor longer HRT, 24 h) and TP (favor intermediate HRT, 18 h); if simultaneous optimization is required, accept a compromise around 18–20 h HRT.

Ansatzpunkte6

Konkrete Lücken in dieser Publikation, jeweils mit einem Experiment, das sie schließen würde.

  • Hoch No measurement of N2O or NO2− accumulation during optimization; paper does not report whether nitrification proceeds to NO3− or accumulates at intermediate oxidation states.

    Section 3.1.2 mentions 'simultaneous nitritation/denitritation (SND)' as a potential pathway but provides no data on NO2− or N2O concentrations. High ammonia (>40 mg/L) is known to inhibit NOB, which could lead to NO2− accumulation, but this is not measured.

    Versuch. Measure NO2−-N, NO3−-N, and N2O in effluent across the HRT and ammonia concentration ranges tested (12–24 h, 20–80 mg/L); quantify whether NOB inhibition at high ammonia leads to incomplete nitrification or N2O production.

  • Hoch No explicit measurement of cathode potential, anode potential, or current density during optimization; paper does not report electrochemical operating window.

    Methods section states 'copper wire between the two electrodes and a 200 Ω fixed resistor were connected' but no potentiostat data, voltage profiles, or current density (A/m²) are reported. Nitrogen removal mechanisms (nitrification, denitrification, electrochemical reduction) depend on electrode potentials.

    Versuch. Measure cathode and anode potentials (vs. Ag/AgCl) and current density (mA/m²) at each HRT and ammonia concentration condition; correlate with NH4+-N and NO3−-N removal rates to identify electrochemical vs. biological contributions.

  • Hoch No investigation of dissolved oxygen (DO) concentration in cathode chamber; paper does not report whether aerobic nitrification or oxygen-limited denitrification dominates.

    Methods state 'The cathode chamber was aerated and oxygenated with an air pump' but no DO setpoint, measurement, or profile is given. DO is critical for nitrification kinetics and for distinguishing nitrification from electrochemical reduction pathways.

    Versuch. Measure DO in cathode chamber (mg/L or % saturation) at each condition; vary DO setpoint (e.g., 2, 5, 8 mg/L) to determine optimal window for nitrification vs. denitrification and to assess trade-off between power generation and nitrogen removal.

  • Mittel No measurement of catholyte pH during operation; paper does not report pH profile or buffer capacity, which affect nitrifier activity and ammonia speciation (NH3 vs. NH4+).

    Synthetic wastewater includes 750 mg/L NaHCO3 buffer, but no pH data are reported during the 85 d operation. Nitrification consumes alkalinity and lowers pH; high pH favors NH3 (toxic to nitrifiers) while low pH favors NH4+ (less bioavailable). This is a critical control variable.

    Versuch. Monitor catholyte pH continuously or daily across the optimization range; measure ammonia speciation (NH3 vs. NH4+) using pH-dependent equilibrium calculations; determine if pH drift limits nitrification at high ammonia concentrations.

  • Mittel No analysis of phosphorus speciation or mechanism of TP removal; paper does not distinguish between biological uptake, chemical precipitation, or electrochemical reduction.

    TP removal is reported (59.39%) but no data on PO4³−, HPO4²−, or H2PO4− concentrations, nor on whether phosphorus is removed via biomass accumulation, struvite precipitation, or cathode reduction. Mechanism is unclear.

    Versuch. Measure soluble reactive phosphorus (SRP) and particulate phosphorus in effluent; perform mass balance on phosphorus in biomass and precipitate; test whether TP removal correlates with Mg²+ or Ca²+ concentration (struvite/apatite formation).

  • Mittel No long-term stability or repeated batch testing; paper reports only 85 d operation and does not assess whether optimized conditions are sustainable or if microbial community shifts over longer timescales.

    Microbial community analysis is performed at day 85 only; no time-series data on community succession or performance drift. Optimization is validated over 3 days of continuous operation, which is short for assessing robustness.

    Versuch. Operate optimized systems for ≥6 months; sample microbial community and measure NH4+-N, TP, NO2−, NO3− removal rates weekly to assess long-term stability and identify any community drift or performance degradation.

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Was gemacht wurde

Systemtyp
MFC

Was funktioniert hat

Noch keine Ergebniskennzahlen extrahiert.

Zusammenfassung

In order to study the effects of operating conditions on the performance of a microbial fuel cell (MFC) for treating ammonia nitrogen (NH4+-N) and phosphate and the changes in the microbial community under optimized conditions, in this study, the response surface method (RSM) and central composite design (CCD) were used to carry out experiments and construct a model of the system to analyze the influence of the hydraulic retention time (HRT) and initial influent ammonia concentration on NH4+-N and the total phosphorus (TP) removal performance of the MFC, and the changes in the microbial community structure were analyzed. The results showed that: (1) the initial influent ammonia concentration had a greater impact than the HRT; (2) after optimizing the reaction conditions, the actual removal rates of NH4+-N and TP of the system were 94.88% and 59.39% (the predicted values were 90.18% and 56.25%), respectively; and (3) the total number of species in the optimization group decreased, and the richness of the microbial community decreased. The system conducted the orthoselection of the microbial community and optimized the structure of the microbial community. After the optimization, the dominant strains for ammonia and phosphorus removal on the cathode reactor of each system were strengthened at the phylum and genus levels. Under the coaction of the dominant strains, the efficiencies of nitrogen removal and phosphorus removal in the reactor were significantly improved. The performance optimization of and microbial community change in NH4+-N and TP removal in the MFC system were studied using RSM, which was helpful to improve the effect of nitrogen and phosphorus removal.

Schlagwörter

Microbial fuel cellMicrobial population biologyPhosphorusHydraulic retention timeAmmoniaNitrogen

Kennungen

Zeitschrift
Water
Jahr
2022
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