Stability of aerobic granules during long-term bioreactor operation

Aerobic granular sludge technology has been extensively studied over the past 20 years and is regarded as the upcoming new standard for biological treatment of domestic and industrial wastewaters. Aerobic granules (AG) are dense, compact, self-immobilized microbial aggregates that allow better sludge-water separation and thereby higher biomass concentrations in the bioreactor than conventional activated sludge aggregates. This brings potential practical advantages in terms of investment cost, energy consumption and footprint. Yet, despite the relevant advances regarding the process of AG formation, instability of AG during long-term operation is still seen as a major barrier for a broad practical application of this technology. This paper presents an up-to-date review of the literature focusing on AG stability, aiming to contribute to the identification of key factors for promoting long-term stability of AG and to a better understanding of the underlying mechanisms. Operational conditions leading to AG disintegration are described, including high organic loads, particulate substrates in the influent, toxic feed components, aerobic feeding and too short famine periods. These operational and influent wastewater composition conditions were shown to influence the micro-environment of AG, consequently affecting their stability. Granule stability is generally favored by the presence of a dense core, with microbial growth throughout the AG depth being a crucial intrinsic factor determining its structural integrity. Accordingly, possible practical solutions to improve granule long-term stability are described, namely through the promotion of minimal substrate concentration gradients and control of microbial growth rates within AG, including anaerobic, plug-flow feeding and specific sludge removal strategies.     

Functional consortium from aerobic granules under high organic loading rates

Functional bacterial consortiums that effectively tolerate high organic loading rates (OLR) were isolated using an organic shock-loading-to-extinction approach. The aerobic sludge granules were cultivated at low OLR and microbial community was challenged with stepwise increase in organic loadings to isolate functional consortiums. Strain Zoogloea resiniphila and at least two uncultured strains, Acinetobacter sp. clone JT2 and bacterium clone P1D1-516, formed the functional consortium of the aerobic granules present under a high OLR. The loss of these uncultured strains caused protein leakage from granules, thereby destabilizing the granules. The proposed organic shock-loading-to-extinction approach is effective in isolating the functional consortium from aerobic granules under high OLR.     

High organic loading influences the physical characteristics of aerobic sludge granules

Aims:  The effect of high organic loading rate (OLR) on the physical characteristics of aerobic granules was studied.
Methods and Results:  Two column-type sequential aerobic sludge blanket reactors were fed with either glucose or acetate as the main carbon source, and the OLR was gradually raised from 6 to 9, 12 and 15 kg chemical oxygen demand (COD) m⁻³ d⁻¹. Glucose-fed granules could sustain the maximum OLR tested. At a low OLR, these granules exhibited a loose fluffy morphology dominated by filamentous bacteria. At higher OLRs, these granules became irregularly shaped, with folds, crevices and depressions. In contrast, acetate-fed granules had a compact spherical morphology at OLRs of 6 and 9 kg COD m⁻³ d⁻¹, with better settling and strength characteristics than glucose-fed granules at similar OLRs. However, acetate-fed granules could not sustain high OLRs and disintegrated when the OLR reached 9 kg COD m⁻³ d⁻¹.
Conclusions:  The compact regular microstructure of the acetate-fed granules appeared to limit mass transfer of nutrients at an OLR of 9 kg COD m⁻³ d⁻¹. The looser filamentous microstructure of the glucose-fed granules and the subsequent irregular morphology delayed the onset of diffusion limitation and allowed significantly higher OLRs to be attained.
Significance and Impact of the Study:  High organic loading rates are possible with aerobic granules. This research would be helpful in the development of aerobic granule-based systems for high-strength wastewaters.     

Influence of substrate surface loading on the kinetic behaviour of aerobic granules

In the aerobic granular sludge reactor, the substrate loading is related to the size of the aerobic granules cultivated. This study investigated the influence of substrate surface loading on the growth and substrate-utilization kinetics of aerobic granules. Results showed that microbial surface growth rate and surface biodegradation rate are fairly related to the substrate surface loading by the Monod-type equation. In this study, both the theoretical maximum growth yield and the Pirt maintenance coefficient were determined. It was found that the estimated theoretical maximum growth yield of aerobic granules was as low as 0.2 g biomass g^–1 chemical oxygen demand (COD) and 10–40% of input substrate-COD was consumed through the maintenance metabolism, while experimental results further showed that the unit oxygen uptake by aerobic granules was 0.68 g oxygen g^–1 COD, which was much higher than that reported in activated sludge processes. Based on the growth yield and unit oxygen uptake determined, an oxidative assimilation equation of acetate-fed aerobic granules was derived; and this was confirmed by respirometric tests. In aerobic granular culture, about 74% of the input substrate-carbon was converted to carbon dioxide. The growth yield of aerobic granules was three times lower than that of activated sludge. It is likely that high carbon dioxide production is the main cause of the low growth yield of aerobic granules, indicating a possible energy uncoupling in aerobic granular culture.     

Characterization of aerobic granules by microbial density at different COD loading rates

Aerobic granules were cultivated under temporal alternating aerobic and anoxic conditions without the presence of a carrier material in a sequencing batch reactor (SBR) with a high column height/column diameter ratio. The reactor was operated for 6h per cycle (aerobic: 4.75 h, anoxic: 1.25 h). To determine a new parameter for the definition of aerobic granules, a protocol of 4,6-diamidino-2-phenylindole hydrochloride staining and fluorescence image processing was developed. The d(tm) analysis showed that the increase in the chemical oxygen demand (COD) loading rate promoted no more growth of the aerobic granules. It was inconsistent with the results of the analysis of the sludge volume index (SVI) value but matched well with the results of the COD and nitrogen removal of the SBR and the particle size distribution by LS-PSA. The optimum COD loading rate for aerobic granulation in the SBR was 2.52 kg/m(3)d. When d(tm) was correlated with the biomass concentration and the SVI value during the period of granule formation, d(tm) could be used as a more sensitive and accurate parameter for classifying aerobic granules and optimizing the operational conditions for aerobic granulation processes.     

Biodegradation and kinetics of aerobic granules under high organic loading rates in sequencing batch reactor

Biodegradation, kinetics, and microbial diversity of aerobic granules were investigated under a high range of organic loading rate 6.0 to 12.0 kg chemical oxygen demand (COD) m⁻³ day⁻¹ in a sequencing batch reactor. The selection and enriching of different bacterial species under different organic loading rates had an important effect on the characteristics and performance of the mature aerobic granules and caused the difference on granular biodegradation and kinetic behaviors. Good granular characteristics and performance were presented at steady state under various organic loading rates. Larger and denser aerobic granules were developed and stabilized at relatively higher organic loading rates with decreased bioactivity in terms of specific oxygen utilization rate and specific growth rate (μ _overall) or solid retention time. The decrease of bioactivity was helpful to maintain granule stability under high organic loading rates and improve reactor operation. The corresponding biokinetic coefficients of endogenous decay rate (k _d), observed yield (Y _obs), and theoretical yield (Y) were measured and calculated in this study. As the increase of organic loading rate, a decreased net sludge production (Y _obs) is associated with an increased solid retention time, while k _d and Y changed insignificantly and can be regarded as constants under different organic loading rates.     

Mass transfer limit of fluorescent dyes during multicolor staining of aerobic granules

Multicolor fluorescence experiments are conducted to investigate the distributions of extracellular polymeric substances and/or cells in the bioaggregates. Successful staining requires that the dyes could fully stain the targeted substances of bioaggregates in a finite time. The mass transfer limit for one of the four fluorescent dyes, calcofluor white, concanavalin A conjugated with tetramethylrhodamine, Nile red, and SYTO 63, penetrating entire phenol-fed granules or those sectioned at 50 μm thick, was quantitatively determined. The former three dyes sufficiently stained the entire granule within prescribed time intervals. However, the SYTO 63 could not penetrate the 600-μm granule in a finite time. Simplified one-dimensional diffusional model estimated the apparent diffusivity of SYTO 63 in the aerobic granule matrix. This work revealed that each staining scheme should be examined for the possible mass transfer limit of dyes during staining.     

Diffusivity of oxygen in aerobic granules

This work for the first time estimated apparent oxygen diffusivity (D(app)) of two types of aerobic granules, acetate-fed and phenol-fed, by probing the dissolved oxygen (DO) level at the granule center with a sudden change in the DO of the bulk liquid. With a high enough flow velocity across the granule to minimize the effects of external mass transfer resistance, the diffusivity coefficients of the two types of granules were estimated with reference to a one-dimensional diffusion model. The carbon source has a considerable effect on the granule diameter (d) and the oxygen diffusivity. The diffusivity coefficients were noted 1.24-2.28 x 10(-9) m2/s of 1.28-2.50 mm acetate-fed granules, and 2.50-7.65 x 10(-10) m2/s of 0.42-0.78 mm phenol-fed granules. Oxygen diffusivity declined with decreasing granule diameter, in particular, the diffusivity of acetate-fed granules is proportional to the size, whereas the diffusivity of phenol-fed granules is proportional to the square of granule diameter. The existence of large pores in granule, evidenced by FISH-CLSM imaging, was proposed to correspond to the noted size-dependent oxygen diffusivity. The phenol-fed granules exhibited a higher excellular polymer (ECP) content than the acetate-fed granules, hence yielding a lower oxygen diffusivity.     

Changes in structure,activity and metabolism of aerobic granules as a microbial response to high phenol loading

Four column-type sequential aerobic sludge blanket reactors were fed with phenol as the sole carbon and energy source and operated at loading rates of 1.0, 1.5, 2.0 and 2.5 kg phenol m^–3 day^–1. The results indicated that phenol loading exerted a profound influence on the structure, activity and metabolism of the aerobic granules. Compact granules with good settling ability were maintained at loadings up to 2.0 kg phenol m^–3 day^–1, and structurally weakened granules with enhanced production of extracellular polymers and proteins and significantly lower hydrophobicities were observed at the highest loading of 2.5 kg phenol m^–3 day^–1. Specific oxygen uptake rate, catechol 2,3-dioxygenase (C23O) and catechol 1,2-dioxygenase (C12O) activities peaked at a loading of 2.0 kg phenol m^–3 day^–1, and declined thereafter. Granules degraded phenol completely in all four reactors, mainly through the meta cleavage pathway as C23O activities were significantly higher than C12O activities. At the highest loading applied, the anabolism and catabolism of microorganisms were regulated such that phenol degradation proceeded exclusively via the meta pathway, apparently to produce more energy for overstimulation of protein production against phenol toxicity. This work contributes to a better understanding of the ability of aerobic granules to handle high-strength industrial wastewaters containing chemicals that are normally inhibitory to microbial growth.     

Long-term storage and subsequent reactivation of aerobic granules

This study investigated a seven month storage and the subsequent reactivation of aerobic granules. The granule size and structure integrity were remained during storage, whereas some cavities and pleats appeared on the surface and further deteriorated the settleability. Along with the reactivation, the physical characteristics and microbial activities of aerobic granules were gradually improved. Activities of heterotrophs and nitrifiers can be fully recovered within 16days and 11days, respectively. Nitrifiers decayed slower during storage and reinstated rapider during reactivation than heterotrophs. In fresh aerobic granules, the dominated ammonia-oxidizing bacteria (AOB) and nitrite-oxidizing bacteria (NOB) were Nitrosomonas and Nitrospira, respectively. During storage, the initially dominated populations decayed rapider than the initially less dominated ones. Extracellular polymeric substances (EPS) significantly decreased within the first month, and then gradually accumulated during the last six months storage. Accumulation of EPS was an effective strategy for maintaining structural integrity of aerobic granules during long-term storage.     

Transformation of anaerobic granules into aerobic granules and the succession of bacterial community

Applied Microbiology and Biotechnology - In this study, we demonstrated that anaerobic granular sludge could be successfully transformed into aerobic granular sludge in a continuous up-flow reactor...     

Degradation of cresols by phenol-acclimated aerobic granules

High-strength cresol isomers were treated with phenol-acclimated granules in batch experiments. The aerobic granules effectively metabolized cresol isomers at concentrations up to 1,500 mg l⁻¹. The modified Haldane kinetic model, used to assess the kinetic behavior during cresol degradation by granule cells, yielded a high maximum specific growth rate (1.13–1.45 h⁻¹) and inhibition constant (617–952 mg l⁻¹). The microbial community structure, which was stable under cresol stress, was principally composed of genera Bacillus, Acinetobacter, Corynebacterium, and Nocardioides. Enzyme assay results suggest simultaneous expression of ortho- and meta-cleavage pathways during cresol degradation. Under high cresol concentrations, however, cresol isomers were largely degraded via the meta-cleavage pathway, likely attributable to the activity of Bacillus. The aerobic granular sludge system is a promising biotechnology for degrading wastewater containing high-strength cresols.     

The influence of short-term starvation on aerobic granules

Evidence shows that almost all aerobic granules can only be cultivated in sequencing batch reactor (SBR). Compared to continuous process, the unique feature of SBR is its cycle operation, which results in a periodical starvation in the reactor. So far, the effect of such a periodical starvation on aerobic granulation process remains unknown. Thus, this study investigated the responses of aerobic granules to the respective carbon-, nitrogen-, phosphorus-, potassium-starvation and also their collective effects in terms of cell surface hydrophobicity, surface zeta potential, extracelluar polysaccharides content, specific oxygen utilization rate and biomass growth. Results showed that short-term C-, N-, P- and K- starvations would pose negative effects on aerobic granules, e.g. reduce EPS content, inhibit microbial activity, weaken structural integrity and worsen settleability of aerobic granules. This study likely provides primary evidence that the substrate and nutrients starvation would not contribute to the stability of aerobic granules in a significant way.     

Rapid cultivation of stable aerobic phenol-degrading granules using acetate-fed granules as microbial seed

cDNA-encoding pyranose 2-oxidase (P2O) from Trametes pubescens was sequenced and cloned into Escherichia coli strain BL21/DE3 on a multicopy plasmid under the control of trc promoter. The synthesis of P2O was studied in a batch culture in M9-based mineral medium: the enzyme was synthesized constitutively at 28 °C in amount corresponding to 8% of the cell soluble protein (0.6 U mg⁻¹). Only small portion of P2O (11%) was in the form of non-active inclusion bodies. Purified recombinant enzyme has similar physico-chemical and kinetic parameters with other P2Os. When compared to the expression of p2o of Trametes ochracea, a ratio of the mature enzyme to inclusion bodies found in the same E. coli host at 28 °C is as much as nine times higher. The finding makes the enzyme from T. pubescens preferable for the large-scale production by recombinant bacteria. The difference in amino acid sequences of the P2O from T. ochracea and T. pubescens may explain the favourable trait of the latter enzyme regarding protein folding.     

Distribution of extracellular polymeric substances in aerobic granules

Extracellular matrix provides an architectural structure and mechanical stability for aerobic granules. Distributions of cells and extracellular polymeric substances (EPS), including proteins, α- and β-d-glucopyranose polysaccharides, in acetate-fed granules and phenol-fed granules were probed using a novel quadruple staining scheme. In acetate-fed granules, protein and β-d-glucopyranose polysaccharides formed the core, whereas, the cells and α-d-glucopyranose polysaccharides accumulated in the granule outer layers. Based on these experimental findings, this study indicated that different conclusions can be obtained regarding EPS distributions when granules were stained differently. The core of phenol-fed granules, conversely, was formed principally by proteins; whereas, the cells and α- and β-d-glucopyranose polysaccharides were accumulated at an outer filamentous layer. Using a series of confocal laser scanning microscope (CLSM) images whose threshold values were determined via Otsu’s scheme, the three-dimensional distributions of cells and EPS were produced using a polygonal surface model. Structural information extracted can be applied in further development of comprehensive granule models.     

Characterization and evaluation of aerobic granules in sequencing batch reactor

In order to investigate the aerobic granules cultured under alternating aerobic and anoxic conditions, a sequencing batch reactor (SBR) was operated without the presence of a carrier material. Nitrification and denitrification occurred alternately in the SBR operation, with an increased nitrification efficiency of up to 97% and a high chemical oxygen demand (COD) removal efficiency of up to 95%. It was observed that physical characteristics of granule play an important role in the performance of the SBR process. Light microscopy was used to observe the time dependent development of the granules in the SBR. Based on the microscopic observations, some floc-like sludges remained in the form of a mixture with granules for 30 days of operation. Even though various granule sizes had been formed in the reactor after 50 days, the granule sizes were primarily from 1 +/- 0.35 to 1.3 +/- 0.45 mm, rarely exceeding 2 mm. The granules were analyzed by a combination of microelectrodes and fluorescent in situ hybridization (FISH), which provides more detailed information on what happens inside the granules. Based on their results, ammonia oxidizing bacteria (AOB) existed primarily in the upper and middle layers of the granule. Assuming a first-order reaction for nitrification, most of the nitrification is likely to occur from the surface to 300 microm into the granular thickness.     

Distribution of EPS and cell surface hydrophobicity in aerobic granules

This study described the distribution of extracellular polysaccharides (EPS) and hydrophobicity in aerobic granule as well as the essential role of EPS in maintaining the stable structure of aerobic granules. Aerobic granules showed a heterogeneous structure, which had an outer shell with high biomass density and an inner core having a relatively low biomass density. Results showed that the outer shell of aerobic granule was composed of poorly soluble and noneasily biodegradable EPS, whereas its core part was filled with readily soluble and biodegradable EPS. It was further found that the shell of aerobic granule exhibited a higher hydrophobicity than the core of granule. The insoluble EPS present in the granule shell would play a protective role with respect to the structure stability and integrity of aerobic granules.     

Carbon,nitrogen and phosphorus removal mechanisms of aerobic granules

Aerobic granules are the potential tools to develop modern wastewater treatment technologies with improved nutrient removal efficiency. These granules have several promising advantages over conventional activated sludge-based wastewater treatment processes. This technology has the potential of reducing the infrastructure and operation costs of wastewater treatment by 25%, energy requirement by 30%, and space requirement by 75%. The nutrient removal mechanisms of aerobic granules are slightly different from that of the activated sludge. For instance, unlike activated sludge process, according to some reports, as high as 70% of the total phosphorus removed by aerobic granules were attributed to precipitation within the granules. Similarly, aerobic granule-based technology reduces the total amount of sludge produced during wastewater treatment. However, the reason behind this observation is unknown and it needs further explanations based on carbon and nitrogen removal mechanisms. Thus, as a part of the present review, a set of new hypotheses have been proposed to explain the peculiar nutrient removal mechanisms of the aerobic granules.     

Microbial community of acetate utilizing denitrifiers in aerobic granules

Nitrite accumulates during biological denitrification processes when carbon sources are insufficient. Acetate, methanol, and ethanol were investigated as supplementary carbon sources in the nitrite denitrification process using biogranules. Without supplementary external electron donors (control), the biogranules degraded 200 mg l⁻¹ nitrite at a rate of 0.27 mg NO₂–N g⁻¹ VSS h⁻¹. Notably, 1,500 mg l⁻¹ acetate and 700 mg l⁻¹ methanol or ethanol enhanced denitrification rates for 200 mg l⁻¹ nitrite at 2.07, 1.20, and 1.60 mg NO₂–N g⁻¹ VSS h⁻¹, respectively; these rates were significantly higher than that of the control. The sodium dodecyl sulfate polyacrylamide gel electrophoresis of the nitrite reductase (NiR) enzyme identified three prominent bands with molecular weights of 37–41 kDa. A linear correlation existed between incremental denitrification rates and incremental activity of the NiR enzyme. The NiR enzyme activity was enhanced by the supplementary carbon sources, thereby increasing the nitrite denitrification rate. The capacity of supplementary carbon source on enhancing NiR enzyme activity follows: methanol > acetate > ethanol on molar basis or acetate > ethanol > methanol on an added weight basis.