Relations between substrate feeding pattern and development of filamentous bacteria in activated sludge processes

Summary Laboratory scale activated sludge systems were operated under regimes of continuous or intermittent feeding of substrate. It was found that continuously fed systems repeatedly resulted in the development of filamentous bacteria and bulking of the sludge. Intermittently fed systems did form good settling sludges, without filamentous bacteria. The same results were found using different sludge loadings and different concentrations of mixed liquor suspended solids. High dissolved oxygen concentration did not prevent bulking in continuous systems while low dissolved oxygen concentration resulted in bulking with intermittently fed systems. It was found that the substrate removal rate of intermittently operated systems was always higher than for continuously fed systems. The hypothesis is formulated that intermittent feeding leads to higher substrate removal rates by floc forming bacteria and their predominance in intermittently fed systems, which can be compared to plug flow systems.     

Relations between substrate feeding pattern and development of filamentous bacteria in activated sludge processes:

Summary Laboratory scale activated sludge systems were operated under regimes of continuous or intermittent feeding of substrate. In a previous paper it was shown that continuously operated systems resulted in the development of filamentous bacteria and bulking sludges. Intermittently fed sludges resulted in good settling. These results are now confirmed when substrates other than glucose are present in the influent, such as nutrient broth, acetate and starch. With casein deflocculation occurred. For intermittent systems the substrate removal rates were higher than for continuous systems. Based on the results a theory is presented to account for the growth of filamentous bacteria (and bulking) in continuous systems (completely mixed systems). This theory assumes that in intermittently fed systems (plug flow systems) floc forming bacteria become dominant as a result of higher substrate uptake rates and the possibility to survive a starvation phase by thriving on accumulated intracellular metabolites.     

Stable limited filamentous bulking through keeping the competition between floc-formers and filaments in balance

Limited filamentous bulking (LFB) was proposed to save aeration energy consumption and enhance the capacity of filaments to degrade substrates with low concentrations in activated sludge systems. Operational parameters favorable for maintaining the LFB state were investigated in an anoxic-oxic reactor treating domestic wastewater. The experiments showed that the LFB state would deteriorate with sharply decreasing temperature, reducing substrate gradients or removing anoxic zones. The balance between filaments and floc-formers could be achieved by controlling dissolved oxygen and sludge loading rates to be in optimal ranges. Eikelboom Type 0041 and CandidatusMicrothrix parvicella were the filamentous bacteria responsible for the LFB state. However, the excess growth of Eikelboom Type 021N and Sphaerotilus natans were observed when serious bulking occurred under low substrate gradients. It was demonstrated that stable maintenance of LFB for energy saving was feasible by process control and optimization.     

Bulking sludge in biological nutrient removal systems

Bulking sludge problems are commonly reported in biological nutrient removal (BNR) systems. This has led to the general belief that intrinsic BNR conditions favor the growth of undesirable and excessive filamentous bacteria. The present study shows that other factors have a major role in bulking, and not the BNR conditions. These factors have been verified in well-controlled, strictly anoxic-aerobic and strictly anaerobic-aerobic sequencing batch reactor systems. The experimental results show that conditions known to be responsible for bulking sludge in aerobic systems (i.e., low concentration of electron donor and/or electron acceptor) did not lead to bulking. Even when acetate was present at very low concentrations in the aerobic stage of an anaerobic-aerobic bio-P system, the sludge settleability remained very good. This clearly demonstrates that good bio-P activity can stabilize and improve sludge settleability. The presence of microaerophilic conditions in the anoxic stage of the anoxic-aerobic system was the only factor leading to worsening sludge settling characteristics. The results are discussed in light of our previous hypothesis about the importance of diffusion-limited substrate uptake for the development of filamentous structures in biological flocs. The hypothesis is extended to anaerobic-aerobic and anoxic-aerobic conditions, typical of BNR-activated sludge systems. Taking into account the effect of feeding patterns on biochemical rates and on the development of filamentous bacterial structures, we recommend the adoption of plug-flow selector configurations, with strictly anaerobic and/or strictly anoxic conditions, wherein microaerophilic conditions are excluded, in order to maintain reliable and robust BNR performance.     

Monitoring filamentous bulking in activated sludge systems fed by synthetic or municipal wastewater

The stability with respect to filamentous bulking of two activated sludge fully-aerobic systems, one with a completely mixed tank and one with a channel reactor, fed either by a synthetic wastewater or by a primary-settled municipal wastewater, of variable composition and flow rate, has been investigated. The morphological characteristics of the biomass in terms of floc size and roughness and of filamentous bacteria abundance have been monitored by image analysis. Severe bulking was only observed in the well-mixed tank fed at a constant flow rate by synthetic substrate of constant concentration, when the channel reactor fed in a similar manner was fully stable. Variations of biomass characteristics as well as of settling properties were observed on both systems fed with the real wastewater, but these events were related to the characteristics of the wastewater, as similar changes were observed on the full-scale plant fed with the same substrate. In any case, automated image analysis was an efficient way to monitor in detail the fate of the activated sludge at pilot and full scale.     

Plug flow simulating and completely mixed reactors with a premixing tank,in the control of filamentous bulking

Summary A sequence of a substrate rich and substrate starvation phase (feast and famine strategy) is created in both compartmentalized reactors and reactors with premixing tanks. This condition is known to be essential in the control of bulking. With a synthetic waste water containing glucose a reactor with 12 compartments was effective in the control of filamentous bulking. With a dairy industrial waste water, containing a slowly biodegradable COD-fraction, this reactor could not suppress the growth of filamentous bacteria. With dairy and brewery waste water, reactors with premixing tanks were used to create a more pronounced exogenous (substrate rich) phase. Using three or more premixing tanks filamentous bulking could be controlled. During the exogenous phase the floc-forming microorganisms, having a higher substrate uptake rate, can take up the largest amount of substrate and can survive better during the endogenous phase.Substrate concentration and respiration rate profiles were studied and the concentration of the reserve materials was monitored.For each type of waste water the sludge loading and the fraction of readily available COD will determine the system's design.     

Genomic insights into Candidatus Amarolinea aalborgensis gen. nov., sp. nov., associated with settleability problems in wastewater treatment plants

Settleability of particles in activated sludge systems can be impaired by an overgrowth of filamentous bacteria, a problem known as bulking. These filaments are often members of the phylum Chloroflexi, sometimes reaching abundances in excess of 30% of the biovolume. The uncultured Chloroflexi phylotype, Candidatus Amarolinea, has been observed in high abundances in Danish full-scale activated sludge systems by 16S rRNA gene amplicon surveys, where it has been associated with bulking. In this study, fluorescence in situ hybridization was applied to confirm their high abundance, filamentous morphology, and contribution to the interfloc bridging that characterizes filamentous bulking. Furthermore, genome-centric metagenomics using both Illumina and Oxford Nanopore sequencing was used to obtain a near complete population genome (5.7 Mbp) of the Ca. Amarolinea phylotype, which belongs to the proposed novel family Amarolineaceae within the order Caldilineales of Chloroflexi. Annotation of the genome indicated that the phylotype is capable of aerobic respiration, fermentation, and dissimilatory nitrate reduction to ammonia. The genome sequence also gives a better insight into the phylogenetic and evolutionary relationships of the organism. The name Candidatus Amarolinea aalborgensis is proposed for the species.     

Effects of synthetic polymer on the filamentous bacteria in activated sludge

Filamentous bulking is one of the solid-liquid separation problems always seen in activated sludge process. The addition of synthetic polymer is always one of the popular ways for the treatment plant operator to immediately solve the poor sludge settling problem. Therefore, it may be interesting to understand the effects of synthetic polymer on the filamentous bacteria in activated sludge. In this study, synthetic polymer was applied to a lab-scale wastewater treatment system with the filamentous bulking problem. The population structure of filamentous bacteria and sludge characteristics were investigated under different conditions. When synthetic polymer was added into the system, it was found that poor sludge settleability caused by filamentous bulking was temporarily solved and filamentous branches growing outside the flocs were damaged or inhibited. However, filamentous growth was still observed inside the flocs. After the addition of polymer was halted, filamentous branches extended out of the flocs immediately. Very serious filamentous bulking occurred and sludge settleability became much worse than that occurring before the addition of polymer. And, it took several weeks for the system to return to normal operation.     

Ecophysiology of uncultured filamentous anaerobes belonging to the phylum KSB3 that cause bulking in methanogenic granular sludge

A filamentous bulking of a methanogenic granular sludge caused by uncultured filamentous bacteria of the candidate phylum KSB3 in an upflow anaerobic sludge blanket (UASB) system has been reported. To characterize the physiological traits of the filaments, a polyphasic approach consisting of rRNA-based activity monitoring of the KSB3 filaments using the RNase H method and substrate uptake profiling using microautoradiography combined with fluorescence in situ hybridization (MAR-FISH) was conducted. On the basis of rRNA-based activity, the monitoring of a full-scale UASB reactor operated continuously revealed that KSB3 cells became active and predominant (up to 54% of the total 16S rRNA) in the sludge when the carbohydrate loading to the system increased. Batch experiments with a short incubation of the sludge with maltose, glucose, fructose, and maltotriose at relatively low concentrations (approximately 0.1 mM) in the presence of yeast extract also showed an increase in KSB3 rRNA levels under anaerobic conditions. MAR-FISH confirmed that the KSB3 cells took up radioisotopic carbons from [(14)C]maltose and [(14)C]glucose under the same incubation conditions in the batch experiments. These results suggest that one of the important ecophysiological characteristics of KSB3 cells in the sludge is carbohydrate degradation in wastewater and that high carbohydrate loadings may trigger an outbreak of KSB3 bacteria, causing sludge bulking in UASB systems.     

Bacteriophage-based biocontrol of biological sludge bulking in wastewater

In a previous paper, the first ever application of lytic bacteriophage (virus)-mediated biocontrol of biomass bulking in the activated sludge process using Haliscomenobacter hydrossis as a model filamentous bacterium was demonstrated. In this work we extended the biocontrol application to another predominant filamentous bacterium, Sphaerotilus natans, notoriously known to cause filamentous bulking in wastewater treatment systems. Very similar to previous study, one lytic bacteriophage was isolated from wastewater that could infect S. natans and cause lysis. Significant reduction in sludge volume index and turbidity of the supernatant was observed in batches containing S. natans biomass following addition of lytic phages. Microscopic examination confirmed that the isolated lytic phage can trigger the bacteriolysis of S. natans. This extended finding further strengthens our hypothesis of bacteriophage-based biocontrol of overgrowth of filamentous bacteria and the possibility of phage application in activated sludge processes, the world's widely used wastewater treatment processes.     

Bacteriology of activated sludge,in particular the filamentous bacteria

Microscopic examination of bulking activated sludge samples showed the presence of a variety of filamentous microorganisms, some of which have not yet been described in the literature. A method was developed to obtain pure cultures of these threaded bacteria. To date, five clearly different groups of filamentous bacteria may be distinguished by the determination of a few morphological and physiological characteristics of the isolates. A variety of sheathed bacteria are included in Group I. Group II includes non-motile, gram-negative, orange- or yellow-pigmented filamentous bacteria. These microorganisms are thought to be related to some species of the genusFlavobacterium. The gram-negative, threaded bacteria of Group III show a more or less distinct gliding movement and form red colonies on rich agar media. These bacteria may apparently be related to species described in the generaMicroscilla andFlexibacter. The filamentous bacteria of Group IV structurally resemble someCyanophyceae, but do not contain photosynthetic pigments. They are gram-positive and non-motile. A number of unknown, non-motile bacteria which stain gram-positive with a variable number of gram-negative autolyzed cells in the filaments, are assigned to Group V. The properties of the isolated bacteria are described briefly and their occurrence in bulking activated sludge is discussed.     

Clarifying the roles of kinetics and diffusion in activated sludge filamentous bulking

We hypothesized that the growth rates of filaments and floc formers in activated sludge are affected by the combination of kinetic selection (Lou and de los Reyes, Biotechnol Bioeng 92(6): 729-739, 2005b) and substrate diffusion limitation (Martins et al., Water Res 37:2555-2570, 2003). To clarify the influence of these factors in explaining filamentous bulking, a conceptual framework was developed in this study. The framework suggests the existence of three different regions corresponding to bulking, non-bulking, and intermediate regions, based on substrate concentration. In the bulking and non-bulking regions, kinetic growth differences control the competition process, and filaments or floc formers dominate, respectively. In the intermediate region, substrate diffusion limitation, determined by the floc size, plays the major role in causing bulking. To test this framework, sequencing batch reactors (SBRs) were operated with influent COD of 100, 300, 600, and 1,000 mg/L, and the sludge settleability was measured at various floc size distributions that were developed using different mixing strengths. The experimental data in the bulking and intermediate regions supported the proposed framework. A model integrating the two factors was developed to simulate the substrate concentrations at different depths and floc sizes under intermittently feeding conditions. The modeling results confirmed that substrate diffusion limitation occurs inside the flocs at a certain range of activated sludge floc sizes over the operation cycle, and provided additional support for the proposed framework.     

Relationship of species-specific filament levels to filamentous bulking in activated sludge

To examine the relationship between activated-sludge bulking and levels of specific filamentous bacteria, we developed a statistics-based quantification method for estimating the biomass levels of specific filaments using 16S rRNA-targeted fluorescent in situ hybridization (FISH) probes. The results of quantitative FISH for the filament Sphaerotilus natans were similar to the results of quantitative membrane hybridization in a sample from a full-scale wastewater treatment plant. Laboratory-scale reactors were operated under different flow conditions to develop bulking and nonbulking sludge and were bioaugmented with S. natans cells to stimulate bulking. Instead of S. natans, the filament Eikelboom type 1851 became dominant in the reactors. Levels of type 1851 filaments extending out of the flocs correlated strongly with the sludge volume index, and extended filament lengths of approximately 6 x 10(8) micro m ml(-1) resulted in bulking in laboratory-scale and full-scale activated-sludge samples. Quantitative FISH showed that high levels of filaments occurred inside the flocs in nonbulking sludge, supporting the "substrate diffusion limitation" hypothesis for bulking. The approach will allow the monitoring of incremental improvements in bulking control methods and the delineation of the operational conditions that lead to bulking due to specific filaments.     

Substrate uptake tests and quantitative FISH show differences in kinetic growth of bulking and non-bulking activated sludge

The competition between filaments and floc formers in activated sludge has been historically described using kinetic selection. However, recent studies have suggested that bacterial storage may also be an important factor in microbial selection, since the dynamic nature of substrate flows into wastewater treatment plants elicit transient responses from microorganisms. Respirometry-based kinetic selection should thus be reevaluated by considering cell storage, and a more reliable method should be developed to include bacterial storage in the analysis of growth of filaments and floc formers in activated sludge. In this study, we applied substrate uptake tests combined with metabolic modeling to determine the growth rates, yields and maintenance coefficients of bulking and non-bulking activated sludge developed in lab scale reactors under feast and famine conditions. The results of quantitative fluorescence in situ hybridization (FISH) showed that the filaments Eikelboom Type 1851, Type 021N, and Thiothrix nivea were dominant in bulking sludge, comprising 42.0 % of mixed liquor volatile suspended solids (MLVSS), with 61.6% of the total filament length extending from flocs into bulk solution. Only low levels of Type 1851 filament length (4.9% of MLVSS) occurred in non-bulking sludge, 83.0% of which grew inside the flocs. The kinetic parameters determined from the substrate uptake tests were consistent with those from respirometry and showed that filamentous bulking sludge had lower growth rates and maintenance coefficients than non-bulking sludge. These results provide support for growth kinetic differences in explaining the competitive strategy of filamentous bacteria.     

Transient behavior and time aspects of intermittently and continuously fed bacterial cultures with regard to filamentous bulking of activated sludge

Summary Pure culture transient experiments with Arthrobacter globiformis and Sphaerotilus natans revealed that the floc-forming species A. globiformis can adapt better to intermittent feeding (I-feeding) than the filamentous species S. natans. The floc-forming bacterium showed a larger overcapacity for substrate uptake, a larger accumulation of reserves (polysaccharides and poly--hydroxybutyric acid) and a more efficient mobilization of these polymers. As a consequence A. globiformis became dominant in an I-fed dual culture of S. natans and A. globiformis. The transient behaviour of filamentous continuously fed (C-fed) sludge was similar to the response of S. natans. Consequently, I-feeding of activated sludge could prevent the excessive growth of filamentous bacteria. I-fed sludge, showed a higher overcapacity, the accumulation of more reserves and a shorter lag phase in protein synthesis than C-fed activated sludge, during the transient response, after a pulse dose of substrate. However, to be effective in the control of bulking, the frequency of I-feeding should allow for a sufficiently long endogenous phase. In addition the available fraction of the COD is important in the optimization of I-feeding as a control strategy for filamentous bulking.     

Quantification of cell-specific substrate uptake by probe-defined bacteria under in situ conditions by microautoradiography and fluorescence in situ hybridization

A technique based on quantitative microautoradiography (QMAR) and fluorescence in situ hybridization (FISH) was developed and evaluated in order to determine the quantitative uptake of specific substrates in probe-defined filamentous bacteria directly in a complex system. The technique, QMAR-FISH, has a resolution of a single cell and is based on an improved fixation protocol and the use of an internal standard of bacteria with known specific radioactivity. The method was used to study the in situ ecophysiology of the filamentous bacteria 'Candidatus Meganema perideroedes' and Thiothrix sp. directly in an activated sludge system. The cellular uptake rate of tritium-labelled substrates revealed an average cell-specific uptake rate of 4.1 yen 10-15 mol of acetate cell-1 h-1 and 3.1 yen 10-15 mol of acetate cell-1 h-1 for the two filamentous species respectively. The two filamentous species had very similar activity in all cells along each filament. Surprisingly, the filaments within both probe-defined populations had threefold variation in activity between the different filaments, demonstrating a large variation in activity level within a single population in a complex system. The substrate affinity (Ks) for uptake of acetate of the cells within the two filamentous bacteria was determined by incubation with variable concentrations of labelled acetate. The Ks values of the 'Candidatus Meganema perideroedes' and the Thiothrix filamentous bacteria were determined to be 1.8 micro M and 2.4 micro M acetate respectively.     

Novel filamentous spore-forming iron bacteria causes bulking in activated sludge

Several Gram-positive iron bacteria were isolated from bulking sludge. They were filamentous and had false branching. They had sheaths with iron deposits and formed spores on modified sucrose casitone yeast extract agar. They did not grow on influsion agar for longer than 1 month but could withstand 80°C for 1 h on the same medium. Adding them to sewage before aeration increased the biochemical oxygen demand of waste water and caused poor settling properties of activated sludges. They were the predominant filamentous micro-organisms in bulking activated sludges. At present, these strains cannot be assigned to recognized taxa of Bacillus spp. or sheathed iron bacteria.     

Sludge bulking impact on relevant bacterial populations in a full-scale municipal wastewater treatment plant

We have investigated the changes of microbial community structures and the concomitant performance in two biological wastewater treatment systems (conventional and inverted A²/O processes) over a whole cycle of sludge bulking. A low level of filament abundance was observed during non-bulking period, with types 0092 and 0041 as the dominant filamentous bacteria. With the increase of the sludge volume index values from 76 (73) to 275 (300) mg/L, the filament abundance estimated by microscopic examination increased from 1 (few) to 5 (abundant), with Microthrix parvicella becoming the dominant filament bacteria. Sludge bulking resulted in a significant shift in bacterial compositions from Proteobacteria to Actinobacteria dominance, characterized by the significant presence of filamentous M. parvicella (from not detected to higher than 60% of clones) and decrease of the dominant Betaproteobacterial population (from higher than 40% to less than 1%). Important relevant bacterial populations including polyphosphate-accumulating organism (PAO, Candidatus Accumulibacter phosphatis), ammonia-oxidizing bacteria (AOB, Nitrosomonas), nitrite-oxidizing bacteria (NOB, Nitrospira) and denitrifying bacteria (Thauera) were absent under the serious bulking condition. Accumulation of nitrite and ammonia was observed during serious bulking, while the phosphorus removal performance was not decreased because M. parvicella could behave as a PAO.     

Predicting the effects of chlorine on the micro-organisms of filamentous bulking activated sludges

Rapid and definite assessment of the effect that a specific biocide has on a specific case of filamentous bulking sludge is a much-needed tool in activated sludge wastewater treatment. The Live/Dead stain (LIVE/DEAD BacLight) distinguishing "living" and "non-living" cells, a nitrifying activity (NA) test and the oxygen uptake rate (OUR) measurement were examined for their appropriateness to predict the effects of chlorine on filamentous bulking sludges. The study showed the live/dead stain to be relevant for revealing the specific effect of chlorine on the filamentous bacteria of a bulking sludge. However, using live/dead stain alone for the determination of the appropriate chlorine dose against bulking may lead to an underestimation of the damage caused by chlorine to the useful microorganisms in the flocs. Indeed, using the live/dead stain, it was not easy to distinguish dead cells caused by chlorination from those originally present in the flocs The NA test was the most sensitive in detecting damage caused by chlorine to the floc-forming microorganisms. Therefore, for a safer determination of the chlorine dose effective against bulking and protective of the microbial activity of the sludge, the results of this study suggest coupling of the live/dead stain with the NA test and/or the OUR test.     

Relationship of Species-Specific Filament Levels to Filamentous Bulking in Activated Sludge

To examine the relationship between activated-sludge bulking and levels of specific filamentous bacteria, we developed a statistics-based quantification method for estimating the biomass levels of specific filaments using 16S rRNA-targeted fluorescent in situ hybridization (FISH) probes. The results of quantitative FISH for the filament Sphaerotilus natans were similar to the results of quantitative membrane hybridization in a sample from a full-scale wastewater treatment plant. Laboratory-scale reactors were operated under different flow conditions to develop bulking and nonbulking sludge and were bioaugmented with S. natans cells to stimulate bulking. Instead of S. natans, the filament Eikelboom type 1851 became dominant in the reactors. Levels of type 1851 filaments extending out of the flocs correlated strongly with the sludge volume index, and extended filament lengths of approximately 6 × 10⁸ μm ml⁻¹ resulted in bulking in laboratory-scale and full-scale activated-sludge samples. Quantitative FISH showed that high levels of filaments occurred inside the flocs in nonbulking sludge, supporting the “substrate diffusion limitation” hypothesis for bulking. The approach will allow the monitoring of incremental improvements in bulking control methods and the delineation of the operational conditions that lead to bulking due to specific filaments.