Limited understanding of the thermal properties and flammability of extracellular polymeric substances (EPS) from municipal sludge has constrained their use in fire safety applications. This study investigates the thermal stability and flame retardancy of EPS derived from secondary sludge, waste sludge, and digested sludges. Comprehensive analyses of chemical composition, activation energy, char formation, and heat and gas release during pyrolysis and combustion reveal potential flame-retardant mechanisms. All EPS from different types of sludge can release both free-radical scavenging compounds and non-flammable gases during combustion to reduce fire propagation in the gas phase. In the condensed phase, EPS demonstrate their char-forming capability as a major flame-retardant mechanism to diminish heat release rate due to the presence of nitrogen, phosphorus, and sulfur elements. While nitrogen-based compounds in EPS contribute to flame-retardant mechanisms in both phases, phosphorus and sulfur mainly act in the condensed phase. Additionally, EPS from secondary sludge show the highest activation energy (372.3 kJ/mol) and ignite 24 s later than other EPS. Cone calorimeter tests confirm that EPS from secondary sludge have superior fire-resistant properties, with increased char contents (31.2 %) and enhanced thermal stability compared to other EPS. This study provides the first comprehensive assessment of EPS as eco-friendly flame retardants, advancing wastewater sludge valorisation and fire safety applications.

城市污水集中收集率是城市污水系统运行效率的关键指标，城市污水污染物排放量是计算城市污水集中收集率的必需参数，但城市污水系统较高溢流量和缺乏溢流监测带来计算城市污水排污量的困扰。为此，应用城市污水系统模型和用水、污水处理、常住人口数等常规市政数据，首次提出了根据污水处理厂进水流量和负荷计算城市污水污染物排放量和污水集中收集率的2种方法。以面积约110 km2、常住居民近100×104 人口的城区污水系统为例，展示了应用2种方法的所需数据、具体步骤和计算结果，分析了2种方法各自的适用性。对流动人口、工商业活动和人日排污量等因素对城市污水污染物排污量的影响和估算进行了讨论。2种方法对当下国内和国外一些国家的城市污水排污量、污水集中收集率的计算和城市污水系统运行效率的评估，具有现实意义。

The centralized collection rate of urban sewage is a key indicator of the operational efficiency of urban sewage systems, urban sewage pollutant loading is an essential parameter for calculating the sewage collection ratio. The high overflow of urban sewage systems and lack of monitoring data pose difficulties in calculating sewage collection ratio. By using the urban sewage system model and regular domestic water consumption and sewage treatment information, this study first time proposed two methods, which were based on the influent flow and pollutant loadings of the sewage treatment plant to calculate the urban sewage pollutant loadings and sewage collection ratio. The applicability of two methods was demonstrated including the required data, specific steps, and calculation results by a case of an urban area with almost 110 km2 square meters and nearly 100×104 inhabitants in a city in the Yangtze Delta area. The applicability of each method was discussed. Furthermore, the effects of the commuters, industry and commercial activities, personal discharge load on the estimation of sewage collection ratio in the cities at different levels of economic development are discussed and analyzed. The methods introduced in this study had practical significance for calculating the sewage collection ratio and evaluating the operation efficiency of urban sewage systems in China and part of the other countries.

Extracellular Polymeric Substances (EPS) are ubiquitous in biological wastewater treatment (WWT) technologies like activated sludge systems, biofilm reactors, and granular sludge systems. EPS recovery from sludge potentially offers a high-value material for the industry. It can be utilized as a coating in slow-release fertilizers, as a bio-stimulant, as a binding agent in building materials, for the production of flame retarding materials, and more. P recovered within the extracted EPS is an intrinsic part of the recovered material that potentially influences its properties and industrial applications. P is present in EPS in different speciation (e.g., P esters, poly-P, ortho-P, etc.). Such P species are already intensively used in the chemical industry to enhance thermal stability, viscoelasticity, emulsification, water-holding capacity, and many other properties of some natural and petroleum-derived polymers. The translation of this knowledge to EPS is missing which prevents the full utilization of phosphorus in EPS. This knowledge could allow us to engineer EPS via phosphorus for specific target properties and applications. In this review, we discuss how P could affect EPS properties based on experiences from other industries and reflect on how these P species could be influenced during the EPS extraction process or in the WWTPs.

Nitrous oxide (N2O) is the third most important greenhouse gas and originates primarily from natural and engineered microbiomes. Effective emission mitigations are currently hindered by the largely unresolved ecophysiological controls of coexisting N2O-converting metabolisms in complex communities. To address this, we used biological wastewater treatment as a model ecosystem and combined long-term metagenome-resolved metaproteomics with ex situ kinetic and full-scale operational characterization over nearly 2 years. By leveraging the evidence independently obtained at multiple ecophysiological levels, from individual genetic potential to actual metabolism and emergent community phenotype, the cascade of environmental and operational triggers driving seasonal N2O emissions has ultimately been resolved. We identified nitrifier denitrification as the dominant N2O-producing pathway and dissolved O2 as the prime operational parameter, paving the way to the design and fostering of robust emission control strategies. This work exemplifies the untapped potential of multi-meta-omics in the mechanistic understanding and ecological engineering of microbiomes towards reducing anthropogenic impacts and advancing sustainable biotechnological developments.

The removal of nitrogen from the mature leachate landfills is a major challenge. In this study, a novel aeration control strategy combined with step-wise influent addition was used to successfully implement simultaneous partial nitrification, anaerobic ammonia oxidation and denitrification (SNAD) in a single-stage Sequencing Biofilm Batch Reactor (SBBR) used for nitrogen removal and carbon removal of mature landfill leachate with a low C/N ratio. The SNAD process was rapidly initiated by transitioning from aeration to aeration-anaerobic (OA) phases and stabilized under anaerobic-aeration-anoxic (AOA) conditions. The relative abundance of nitrite-oxidizing bacteria (NOB) in the reactor was consistently suppressed (<0.1 %), while the dominant genus of anaerobic ammonium-oxidizing bacteria (AnAOB), Candidatus Jettenia, reached a relative abundance of 10.9 % in the biofilm. During 160 days of operation with influent NH4+-N up to 600.9 mg/L and COD/TIN of 2.3 ± 0.3, the system achieved 98.3 ± 1.1 % nitrogen removal efficiency and effluent TIN of 10.8 ± 1.3 mg N/L, demonstrating robust synergy among ammonia-oxidizing bacteria (AOB), anammox bacteria, and denitrifying bacteria (DNB). This strategy provides a scalable approach for SNAD system cultivation and sustainable treatment of mature landfill leachate.

To meet the increasing drinking water demand, membrane technologies are used to treat previously unavailable water sources. A byproduct of membrane technologies is the concentrate stream, containing valuable resources in higher concentrations. We studied the recovery of iron from different groundwater matrices and anaerobic reverse osmosis (RO) concentrates via precipitation of vivianite and the co-removal of other common groundwater divalent cations Mn²⁺, Mg²⁺ and Ca²⁺ during vivianite precipitation. The formed precipitates were characterized using X-Ray Diffraction and Scanning Electron Microscopy. Vivianite precipitation removed a maximum of 89 % of Fe²⁺ in raw groundwater and 52 % Fe²⁺ from RO concentrate. Substantial co-removal of Mn²⁺ (max 91 %) and limited co-removal of Mg²⁺ (max 7 %) were found, without hindering Fe removal efficiencies or altering morphological changes of the vivianite crystal. In contrast, co-removal of Ca²⁺ occurred at the expense of iron removal, forming amorphous calcium phosphate precipitates. This study shows the potential of vivianite precipitation for iron recovery across a wide range of groundwater matrices and highlights the need for further research to optimize this novel method to treat concentrate streams that are challenging to dispose of.

The emphasis on phosphorus removal and recovery from wastewater treatment plants has intensified in recent years due to the urgent need to reduce dependency on nonrenewable phosphorus reserves. Enhanced biological phosphorus removal (EBPR), driven by a diverse community of polyphosphate-accumulating organisms with distinct metabolic capabilities, offers several advantages over chemical precipitation methods. These benefits include reduced chemical use, lower sludge volumes, decreased reliance on costly chemical precipitants, and improved phosphorus recovery quality. Recent advancements in recovery technologies now enable efficient phosphorus extraction from digester supernatant, dewatered digested sewage sludge, and sewage sludge ash, each yielding different recovery efficiencies. Despite these advances, a comprehensive assessment of the phosphorus recovery potential from these target streams in conjunction with EBPR remains crucial and has yet to be fully explored.

The objective of this study was to treat different types of industrial wastewaters (milk processing wastewater, soft drink wastewater, and soybean oil plant wastewater) using modified configurations of a bioreactor called one-stage internal dual circulation airlift A2O (DCAL-A2O) bioreactor. The modification involved the use of physical barriers (baffle and packing media) to enhance the anoxic zone of the bioreactor. The study investigated the performance of bioreactors in simultaneously removing carbon, nitrogen, and phosphorus. The bioreactor was designed in three configurations: ordinary, baffled, and hybrid DCAL-A2O bioreactors, depending on the type of manipulation. Different operating conditions, such as hydraulic retention time (HRT), air flow rate (AFR), and anaerobic volume ratio (AVR), were examined simultaneously. The hybrid DCAL-A2O bioreactor was found to be highly suitable for wastewater treatment due to its superior biological performance, ease of operation, and cost-effectiveness when compared to two other bioreactors. The chosen bioreactor demonstrated high performance in terms of TCOD, TN, phosphorus removal efficiencies, and effluent turbidity. Specifically, it achieved removal efficiencies of 97.0% for TCOD, 92% for TN (with a concentration of 179.4 mg/L), 90% for phosphorus (with a concentration of 50.33 mg/L), and an effluent turbidity of 9 NTU. These results were obtained under optimal conditions, which included a HRT of 10 h, an AFR of 2 L/min, and an AVR of 0.464. The unique setup of the bioreactor demonstrated its undeniable ability to effectively treat wastewater from different feeding points. PCR tests confirmed the co-existence of multiple functional bacterial species, including AOB, NOB, denitrifying bacteria, anammox, PAOs, DPAOs, and GAOs. This provides strong evidence for concurrent removal of organics and nutrients in all three configurations of the integrated unit. In summary, this study emphasizes the need for ongoing research in energy efficiency to safeguard our environmental resources.

Microorganisms encoding for the N2O reductase (NosZ) are the only known biological sink of the potent greenhouse gas N2O and are central to global N2O mitigation efforts. Clade II NosZ populations are of particular biotechnological interest as they usually feature high N2O affinities and often lack other denitrification genes. We focus on the yet-unresolved ecological constraints selecting for different N2O-reducers strains and controlling the assembly of N2O-respiring communities. Two planktonic N2O-respiring mixed cultures were enriched at low dilution rates under limiting and excess dissolved N2O availability to assess the impact of substrate affinity and N2O cytotoxicity, respectively. Genome-resolved metaproteomics was used to infer the metabolism of the enriched populations. Under N2O limitation, clade II N2O-reducers fully outcompeted clade I affiliates, a scenario previously only theorized based on pure-cultures. All enriched N2O-reducers encoded and expressed the sole clade II NosZ, while also possessing other denitrification genes. Two Azonexus and Thauera genera affiliates dominated the culture, and we hypothesize their coexistence to be explained by the genome-inferred metabolic exchange of cobalamin intermediates. Under excess N2O, clade I and II populations coexisted; yet, proteomic evidence suggests that clade II affiliates respired most of the N2O, de facto outcompeting clade I affiliates. The single dominant N2O-reducer (genus Azonexus) notably expressed most cobalamin biosynthesis marker genes, likely to contrast the continuous cobalamin inactivation by dissolved cytotoxic N2O concentrations (400 μM). Ultimately, our results strongly suggest the solids dilution rate to play a pivotal role in controlling the selection among NosZ clades, albeit the conditions selecting for genomes possessing the sole nosZ remain elusive. We furthermore highlight the potential significance of N2O-cobalamin interactions in shaping the composition of N2O-respiring microbiomes.

While nowadays a lot of measurements are conducted at wastewater treatment plants, data reliability could further be improved, e.g., through data reconciliation. This study demonstrated the added value of data reconciliation to improve data quality in a full-scale wastewater treatment plant. Also, the effect of the mass balance setting (linear and bilinear mass balances) was quantitatively evaluated, considering data sets with missing measurements and with gross errors. The improvement in the precision of the key variables was higher with bilinear mass balances (40–80 %) compared to the linear setting (0–70 %). Besides, it delivered a higher number of improved key variables, especially when flow measurements were limited (minimum improved variables of 15 and 0, respectively). Bilinear mass balances were also more efficient in gross error detection and played a crucial role in cross-validation based on flow measurements, resulting in lower incorrectly-identified gross errors. Overall, it is recommended to use bilinear mass balances.

Aerobic granular sludge (AGS) technology holds great promise of becoming the standard for biological wastewater treatment due to its lower energy consumption, small footprint, and high removal efficiency of nutrients compared to the conventional activated sludge processes. Different-sized aggregates have been shown to harbor a different microbial community composition. The central question is do full-scale AGS wastewater treatment plants (WWTPs) select for core microbial communities across different aggregate sizes and how these selected organisms differ between the different-sized aggregates. This study analyzed samples from nine geographically distributed full-scale AGS WWTPs that consistently perform well in terms of chemical oxygen demand (COD) and nutrient (N and P) removal. The main results showed that site-specific conditions highly influence microbial composition in smaller aggregates (< 1 mm), while larger granules form stable communities independent of WWTP location. Notably, all aggregates contained a small subset of 128–139 core OTUs that were both prevalent and abundant across all sizes. These core OTUs include key functional groups such as fermenters, aerobic heterotrophs, polyphosphate-accumulating organisms (PAOs), glycogen-accumulating organisms (GAOs), and nitrifiers, which play a crucial role in COD and nutrient removal. Additionally, an enrichment pattern was observed, with aerobic heterotrophs dominating in flocs, PAOs in small granules, and GAOs and nitrifiers in large granules. This study offers valuable insights into the core microbiome of different-sized aggregates in full-scale AGS WWTPs and highlights their potential role in overall system performance.

An interesting and potential property of extracellular polymeric substances (EPS) is the hydrogel formation with calcium ions. Aiming at understanding the significant difference in the hydrogel formed between EPS from flocculent and granular sludge, a targeted investigation of the lipopolysaccharides (LPS), one of the important EPS components, was performed. LPS was isolated from the EPS of flocculent and granular sludge, and both the glycan and the lipid A parts of LPS were characterized and compared. The morphology of LPS-calcium (LPS-Ca) aggregates were visualized by the polymyxin B-based fluorescent probe. The LPS constituted about 25 % and 15 % of the EPS from flocculent and granular sludge, respectively. The flocculent sludge LPS showed a lower amount of glycans, shorter glycan chain length, lower molecular weight, and higher possibility of containing unsaturated lipids than the granular sludge EPS. The flocculent sludge LPS-Ca aggregates demonstrated invert structures with the water phase in between, contributing to the fluid-like property of the respect EPS-Ca. In contrast, with the remarkably different chemical structure, LPS-Ca aggregates from granular sludge displayed bilaminar multilayered morphology, contributing to the solid, self-standing hydrogel of EPS-Ca.

The role of high-pH conditions in anaerobic digestion (AD) has traditionally been confined to it's use in pre-treatment processes. However, operating AD at elevated pH and alkalinity offers significant advantages, including in-situ upgrading of biogas to biomethane. This study examines the potential and scalability of AD under these conditions (pH ∼ 9.3; alkalinity ∼ 0.5 eq/L). The substrate used was the alkaline waste generated from the extraction of extracellular polymeric substances (EPS) from aerobic granular sludge (AGS), and the inoculum used was a haloalkaliphile microbial community from soda lake sediments. To evaluate the system’s performance, the organic loading rate (OLR) was incrementally increased. The highest methane production obtained was 8.4 ± 0.1 mL/day/gVSadded at a hydraulic retention time (HRT) of 15 days and an OLR of 1 kgVS/day/m3. At this loading rate, methanogenesis became the rate limiting conversion. The maximum volatile solids conversion was 48.1 ± 1.1 %. Throughout the reactor operation, methane purity in the biogas consistently exceeded 90 % peaking at 96.0 ± 0.2 %, showcasing the potential for in-situ biogas purification under these conditions. In addition, no ammonia inhibition was observed, even with free-ammonia (NH3) concentrations reaching up to 14 mM. This study underscores the potential of high-pH anaerobic digestion as a sustainable method for both waste treatment and energy recovery.

Within this research, a one-stage hybrid dual internal circulation airlift A2O (DCAL-A2O) bioreactor was designed and operated to simultaneously remove carbon, nitrogen and phosphorous (CNP) from milk processing wastewater (MPW) in different operational circumstances. The substantial operating variables monitored in this work were including hydraulic retention time (HRT), airflow rate (AFR) and aeration volume ratio (AVR) ranged from 7 to 15 h, 1–3 L/min and 0.324–0.464, respectively. From the view point of economics and process function, the optimum conditions were obtained at the HRT, AFR and AVR of 10 h, 2 L/min and 0.464, respectively. At the optimum conditions TCOD, TN, TP removal efficiencies and effluent turbidity were reported to be 97 %, 90 %, 92 % and 9 NTU, respectively. The impact of wastewater biodegradability (BOD5/COD) was evaluated on the bioreactor performance using two other wastewaters i.e. soft drink (SDW) and soybean oil plant wastewaters (SOW) in comparison with the MPW. Removal efficiencies for TCOD and TN exceeding 80 % were observed. The feeding location revealed a prominent impact on the TN and phosphorous removal efficiencies (both ≥80 %) related to the availability degree of the readily biodegradable organic substrate to denitrifiers and PAOs. The rise in HRT, AFR and AVR resulted in reducing microbial secretions as SMP present in sludge and bioreactor effluent as well as loosely bounded EPS (LB-EPS), reported to be 26, 28, 32.5 and 194.4 mg/L TOC, respectively. Different bacteria species were present at optimum conditions confirming concurrent CNP removal in a single body. Finally, the operating cost evaluation verified the effectiveness of the hybrid airlift A2O treating the MPW.

The synthesis of chemically derived bituminous-based activated carbons (ACs) was conducted in this research. The study examined the efficacy of the KOH-2 modified AC by conducting batch experiments under different operating settings. Pollutant concentration, adsorbent dosage and contact time were considered as variables. Bovine serum albumin (BSA), dextrose, and methylene blue (MB) were used as model substances to represent protein, carbon, and textile dyes, respectively. Under optimal conditions, the activated carbon modified with a 2:1 impregnation ratio using KOH showed the best performance among two other ACs, therefore, that was introduced as chosen AC. The optimal parameters were determined as pollutant concentration, adsorbent dosage and contact time obtained to be 600 mg/L, 0.22 g/L and 220 min; 200 mg/L, 0.6 g/L and 180 min; 200 mg/L, 1 g/L and 196 min for MB, BSA and dextrose, respectively. This AC obtained the highest adsorption capacity of 2710.6, 283, and 273 mg/g adsorbing MB, BSA and dextrose, respectively. In the following, column studies were conducted using biologically treated wastewater obtained from a new one-stage hybrid internal circulation airlift A2O bioreactor to eliminate soluble microbial products (SMP). It was seen that the adsorption column, which was filled with the AC under optimal experimental conditions (bed height of 4.5 cm and solution flow rate of 5 mL/min), resulted in a decrease in residual organic substances from 35 mg-TOC/L to 6.6 mg-TOC/L. It is worth mentioning that the utilization of an integrated approach involving sophisticated biological treatment and post-treatment technology has demonstrated efficacy in the elimination of residual organic substances.

Valuable and rare materials in seawater brine are often discarded during desalination. However, there is an increasing focus on recovering these resources, due to the economic and environmental opportunities it can bring. Despite this shift, current Sustainability Assessments (SA) in desalination overlook the brine handling and social dimensions, and brine treatment assessments remain centered on techno-economic dimensions. This work proposes a comprehensive framework for the SA of integrated desalination and resource recovery options, focusing on recovering valuable materials from brine. The framework not only evaluates pre-defined systems but supports the identification of system features of interest, such as products to assess and technologies to include, as well as the transparent selection of indicators, considering specific contexts. To develop this framework, a review of the literature on SA in desalination and brine treatment systems was conducted. Looking at the identified gaps, we synthesized the findings and key messages and proposed the integration of Multi-Criteria Analysis and Value-Sensitive Design in the decision-making process. This allows stakeholders to be involved and incorporates their values at different stages of the assessment, making it distinct from traditional SA methods. This framework offers structured guidance to stakeholders on how to carry out qualitative and quantitative assessments while ensuring transparency in the assessment process.

The implementation of mainstream anaerobic ammonium oxidation (anammox) can facilitate the realization of carbon-neutral wastewater treatment. However, this technology remains challenging owing to the inability to stably provide nitrite. In this study, we developed a novel nitrification and elemental sulfur-based partial autotrophic denitrification/anammox (NS⁰DA) process for mainstream nitrogen removal. The NS⁰DA system consists of a nitrification reactor and a combined elemental sulfur-based denitrification and anammox (S⁰DA) reactor. Each reactor was independently initiated and optimized before being integrated. At mainstream nitrogen levels (48.5 ± 1.7 mg NH₄⁺-N/L) and 25 °C, the NS⁰DA system achieved 89.1 ± 5.7 % total nitrogen (TN) removal efficiency, with an effluent TN concentration of 5.4 ± 2.8 mg N/L. The system exhibited a low N₂O emission factor (0.23 %), significantly lower than other anammox-based systems. The S⁰DA reactor achieved a nitrogen removal rate of 0.53 kg N/(m³·d) with a short hydraulic retention time (2 h). Anammox accounted for 87.3 ± 7.0 % of the TN removal in the S⁰DA reactor. Isotope experiments and kinetic analysis revealed the cooperation between anammox and denitrification for nitrogen removal. Polysulfides formed in the S⁰DA reactor enhanced the utilization rate of elemental sulfur. High-throughput sequencing identified Thiobacillus and Candidatus Brocadia as the dominant genera of sulfur oxidation and anammox, respectively. The nitrogen and sulfur metabolic pathways were further verified through metagenomic analysis. Overall, the NS⁰DA process provides a stable and efficient nitrogen removal process, minimizing oxygen demand, eliminating organic carbon requirements, and reducing N₂O emissions compared to conventional nitrification/denitrification. This approach offers a promising solution for mainstream nitrogen removal in wastewater treatment.

Methane removal is an essential step in drinking water production from methane-rich groundwaters. Conventional aeration-based stripping results in significant direct methane emissions, contributing up to one-third of a treatment plant's total carbon footprint. To address this, a full-scale trickling filter was operated for biological methane oxidation upstream of a submerged sand filter, and its performance was compared to a conventional aeration–submerged sand filtration set-up. Full-scale data were combined with ex-situ batch assays and metagenome-resolved metaproteomics to quantify the individual contribution of the main (a)biotic processes and characterize the enriched microbial communities. Both treatment setups fully removed methane, iron, ammonium, and manganese, yet the underlying mechanisms differed significantly. Methane was completely removed from the effluent after trickling filtration, with stripping and biological oxidation each accounting for half of the removal, thereby halving overall methane emissions. Methane-oxidizing bacteria not only outcompeted nitrifiers in the trickling filter, but also likely contributed directly to ammonia oxidation. In contrast to the submerged filter preceded by methane stripping, signatures of biological iron oxidation were almost completely absent in the trickling filter, suggesting that the presence of methane directly or indirectly promotes chemical iron oxidation. All systems had similar ex-situ manganese oxidation capacities, yet removal occurred only in the submerged filters but not the trickling filter. Ultimately, our results demonstrate that trickling filtration is effective in promoting biological methane oxidation at comparable produced drinking water quality, highlighting its potential for advancing sustainable drinking water production.

The hydrolysis of structural extracellular polymeric substances (St-EPS) is considered a major limiting step in the anaerobic fermentation of waste activated sludge (WAS). However, the degradation of heteropolysaccharides, characterized by complex monomers of uronic acids and neutral saccharides in St-EPS, has rarely been reported. In this study, microbial-produced xanthan-like heteropolysaccharides, characterized by a blue filamentary film, were identified. The xanthan-producing bacteria comprised ∼7.2% of total genera present in WAS. An xanthan-degrading consortium (XDC) was enriched in an anaerobic batch reactor. This consortium could degrade Xanthan for over 90% and disrupt the gel structure of xanthan while promoting methane production from WAS by 29%. The xanthan degradation network consisting of extracellular enzymes and bacteria was elucidated by combining high-throughput sequencing, metagenomic, and metaproteomic analyses. Five enzymes were identified as responsible for hydrolyzing xanthan to monomers, including xanthan lyase, β-D-glucosidase, β-D-glucanase, α-D-mannosidase, and unsaturated glucuronyl hydrolase. Seven genera, including Paenibacillus (0.2%) and Clostridium (3.1%), were identified as key bacteria excreting one to five of the aforementioned enzymes. This study thus provides insights into the complex conversions in anaerobic digestion of WAS and gives a foundation for future optimization of this process.

Groundwater is one of the major sources for drinking water supply worldwide. Conventional iron removal via aeration-filtration produces about 72,802 t of iron sludge annually in the Netherlands alone. Iron sludge comprises low-density flocs of little to no commercial value. The current study explored a novel concept for iron removal, namely anoxic iron sulfides formation in a fixed bed continuous flow reactor. Iron sulfides usually form dense structures and offer a wider range of re-use applications. A packed bed up-flow column reactor filled with pyrite granules was fed iron and sulfide containing solutions. Produced solids were analyzed applying X-ray diffraction analysis, Raman spectroscopy, digital microscopy, scanning electron microscopy and energy dispersive X-ray spectroscopy. Rapid iron sulfides formation was observed after < 10 min. The formed minerals were partially retained by the pyrite granules. The molar ratio of removed Fe(II) to removed S(-II) equaled up to 0.76 ± 0.16 mol Fe(II)_rem/(mol S(-II)_rem). Our results show that iron sulfides formation can present an interesting alternative to iron removal via aeration-filtration due to its compact particle sizes and fast formation rates.