Organic carbon source excites extracellular polymeric substances to boost Fe0-mediated autotrophic denitrification in mixotrophic system

Maximizing the efficiency of single-stage partial nitrification/Anammox granule processes and balancing microbial competition using insights of a numerical model study

Granulation is an efficient approach for the rapid growth of anaerobic ammonia oxidation (Anammox) bacteria (X ANA $$ {X}_{ANA} $$ ) to limit the growth of nitrite-oxidizing bacteria (X NOB $$ {X}_{NOB} $$ ). However, the high sensitivity of Anammox bacteria to operational conditions and the competition with other microorganisms lead to a critical challenge in maintaining sufficientX ANA $$ {X}_{ANA} $$ population. In this study, a one-dimensional steady-state model was developed and calibrated to investigate the kinetic constants ofX ANA $$ {X}_{ANA} $$ growth and mass transport in individual granules, including the liquid film. According to the model calibration results, the range of the maximum specific growth rate constant ofX ANA $$ {X}_{ANA} $$ (μ ANA $$ {\mu}_{ANA} $$ ) was 0.033 to 0.10 d-1. In addition the other kinetic constants ofX ANA $$ {X}_{ANA} $$ were 0.003 d-1 for decay rate constant (b ANA $$ {b}_{ANA} $$ ), 0.10 mg-O2/L for oxygen half-saturation constant (K O 2 ANA $$ {K}_{O_2}^{ANA} $$ ), 0.07 mg-N/L for ammonia half-saturation constant (K NH 4 ANA $$ {K}_{NH_4}^{ANA} $$ ), and 0.05 mg-N/L for nitrite half-saturation constant (K NO 2 ANA $$ {K}_{NO_2}^{ANA} $$ ). The model simulation results showed that the dissolved oxygen of about 0.10 mg-O2/L was found to be optimal to maintain highX ANA $$ {X}_{ANA} $$ population. In addition, minimal COD concentration is required to control heterotrophs (X H $$ {X}_H $$ ) and improve ammonia oxidation by ammonia-oxidizing bacteria (X AOB $$ {X}_{AOB} $$ ). It was also emphasized that moderate mixing conditions (L f $$ {L}_f $$ ≅ $$ \cong $$ 100 μm) are preferable to decrease the diffusion of oxygen to the deep layers of the granules, controlling the competition betweenX ANA $$ {X}_{ANA} $$ andX NOB $$ {X}_{NOB} $$ . A single-factor relative sensitivity analysis (RSA) on microbial kinetics revealed thatμ ANA $$ {\mu}_{ANA} $$ is the governing factor in the efficient operation of the single-stage PN/A processes. In addition, it was found that nitrite concentration is a rate-limiting parameter on the success of the process due to the competition betweenX ANA $$ {X}_{ANA} $$ andX NOB $$ {X}_{NOB} $$ . These findings can be used to enhance our understanding on the importance of microbial competition and mass transport in the single-stage PN/A process. PRACTITIONER POINTS: A one-dimensional steady-state model was developed and calibrated for simulating the single-stage partial nitrification/Anammox (PN/A) granule process. Moderate liquid films (L f $$ {L}_f $$ ≅ $$ \cong $$ 100 μm) are preferable for better performance of Anammox growth in single-stage PN/A processes. Moderate dissolved oxygen (DO≅ $$ \cong $$ 0.10 mg-O2/L) is highly recommended for efficient growth of Anammox bacteria in single-stage PN/A granulation. Minimal COD (COD≅ $$ \cong $$ 0) is preferable for successful operation of the single-stage PN/A granule process. Nitrite concentration is a rate-limiting parameter on the competition between Anammox and nitrite-oxidizing bacteria in the single-stage PN/A processes.

Hydrodynamic cultivation of aeration-free oxygenic photogranules is favored by sufficient amounts of organic carbon

Oxygenic photogranules (OPGs) have great potential for the aeration-free treatment of various wastewater, however, the effects of wastewater carbon composition on OPGs remain unknown. This study investigated the hydrodynamic photogranulation in three types of wastewater with the same total carbon concentration but different inorganic/organic carbon compositions, each operated at two replicated reactors. Results showed that photogranulation failed in reactors fed with only inorganic carbon. In reactors with equal inorganic and organic carbon, loose-structured OPGs formed but then disintegrated. Comparatively, reactors treating organic carbon-based wastewater obtained regular and dense OPGs with better settleability, lower effluent turbidity, excellent structural stability, and higher carbon assimilation rate. Sufficient amounts of organic carbon were crucial for the formation and stability of OPGs as they promoted the secretion of extracellular polymeric substances (EPS) and the growth of filamentous cyanobacteria. This study provides a basis for the startup of OPGs process and facilitates its large-scale application.

The influencing mechanism of AD-MEC domesticated sludge to alleviates propionate accumulation and enhances methanogenesis

Anaerobic digestion combined with microbial electrolysis cell (AD-MEC) could maintain stable reactor operation and alleviating the anaerobic digestion (AD) propionate accumulation. In this study, the addition of sludge to AD-MEC was examined as a way to enhance system performance and explore the microbial interaction mechanism after electric field domestication. The results showed that under 1000 and 4000 mg/L propionate, the methane production of the sludge from AD-MEC increased by 34.29 % and 9.70 %, respectively, as compared to the AD sludge. Gompertz fitting analysis showed that sludge after electric field domestication enhancing its continuous methanogenic capacity. Further analysis showed that sludge extracellular electron transfer capacity was enhanced in AD-MEC and that its domesticated granular sludge formed a microbial community function with acid-degrading synergistic methanogenesis. The results of the study may provide theoretical support and optimization strategies for the application of AD-MEC system.

Stimulating extracellular polymeric substances production in integrated fixed-film activated sludge reactor for advanced nitrogen removal from mature landfill leachate via one-stage double anammox

Introducing carbon sources to achieve nitrogen removal from mature landfill leachate not only increases the costs and carbon emissions but also inhibits the activity of autotrophic bacteria. Thus, this study constructed a double anammox system that combines partial nitrification-anammox (PNA) and endogenous partial denitrification-anammox (EPDA) within an integrated fixed-film activated sludge (IFAS) reactor. In this system, PNA primarily contributes to nitrogen removal pathways, achieving a nitrite accumulation rate of 98.23%. The production of extracellular polymer substances (EPS) in the IFAS reactor is stimulated by introducing co-fermentation liquid. Through the utilization of EPS, the system effectively achieves EPDA with the nitrite transformation rate of 97.20%. Under the intermittent aeration operation strategy, EPDA combined with PNA and anammox in the oxic and anoxic stages enhanced the nitrogen removal efficiency of the system to 99.70 ± 0.12%. The functional genus Candidatus kuenenia became enriched in biofilm sludge, while Thauera and Nitrosomonas predominated in floc sludge.