降解苯胺和氯苯胺类污染物好氧污泥颗粒化及微生物种群结构分析

以序批式气提生物反应器(SABR)为平台,研究了苯胺和氯苯胺类有毒有机废水处理过程好氧污泥颗粒化。结果表明,通过缩短污泥沉降时间、逐步提升目标污染物进水负荷,反应器连续运行3个月,最终在污泥沉降时间5min、COD负荷1.0~3.6kg/(m3.d)、苯胺和氯苯胺负荷1kg/(m3.d)条件下实现污泥颗粒化,COD、苯胺和氯苯胺去除率分别稳定在90%、99.9%以上;获得的成熟好氧颗粒粒径在0.45~2.5mm,SOUR稳定在150mgDO/(gVSS·h)以上,颗粒污泥EPS中PN含量为28.0±1.9mg/gVSS,PN/PS比值为6.5mg/mg,苯胺类比降解速率达0.18g/(g·d);应用PCR-DGGE分子指纹图谱技术分析了稳定运行的颗粒化反应器内好氧污泥微生物种群结构,结果表明好氧颗粒内主要细菌分属β-Proteobacteria、γ-Proteobacteria及Flavobacteria等类群,优势菌为Pseudomonas sp.、Flavobacterium sp.;与已获得的降解氯苯胺好氧颗粒相比,苯胺存在下培养获得的好氧颗粒污泥微生物菌群结构更为丰富。     

Applications of Anammox based processes to treat anaerobic digester supernatant at room temperature

The supernatant of an anaerobic digester was treated at 20 °C in two systems. The first one is a two units configuration, conformed by two sequencing batch reactors (SBR), carrying out partial nitrification and Anammox processes, respectively. Partial nitrification was achieved by granular biomass with a mean diameter of 3 mm, operating at a dissolved oxygen concentration of 2.7 mg/L. The combined system allowed the removal of nitrogen loading rates around 0.08 g N/(L d).     

Organics and nitrogen removal and sludge stability in aerobic granular sludge membrane bioreactor

Novel aerobic granular sludge membrane bioreactor (GMBR) was established by combining aerobic granular sludge technology with membrane bioreactor (MBR). GMBR showed good organics removal and simultaneous nitrification and denitrification (SND) performances for synthesized wastewater. When influent total organic carbon (TOC) was 56.8-132.6 mg/L, the TOC removal of GMBR was 84.7-91.9%. When influent ammonia nitrogen was 28.1-38.4 mg/L, the ammonia nitrogen removal was 85.4-99.7%, and the total nitrogen removal was 41.7-78.4%. Moreover, batch experiments of sludge with different particle size demonstrated that: (1) flocculent sludge under aerobic condition almost have no denitrification capacity, (2) SND capacity was caused by the granular sludge, and (3) the denitrification rate and total nitrogen removal efficiency were enhanced with the increased particle size. In addition, study on the sludge morphology stability in GMBR showed that, although some granular sludge larger than 0.9 mm disaggregated at the beginning of operation, the granular sludge was able to maintain the stability of its granular morphology, and at the end of operation, the amount of granular sludge (larger than 0.18 mm) stabilized in GMBR was more than 56-62% of the total sludge concentration. The partial disaggregation of large granules is closely associated with the change of operating mode from sequencing batch reactor (SBR) system to MBR system.     

Aerobic granular sludge formation for high strength agro-based wastewater treatment

The present study investigates the formation of aerobic granular sludge in sequencing batch reactor (SBR) fed with palm oil mill effluent (POME). Stable granules were observed in the reactor with diameters between 2.0 and 4.0 mm at a chemical oxygen demand (COD) loading rate of 2.5 kg COD m⁻³ d⁻¹. The biomass concentration was 7600 mg L⁻¹ while the sludge volume index (SVI) was 31.3 mL g SS⁻¹ indicating good biomass accumulation in the reactor and good settling properties of granular sludge, respectively. COD and ammonia removals were achieved at a maximum of 91.1% and 97.6%, respectively while color removal averaged at only 38%. This study provides insights on the development and the capabilities of aerobic granular sludge in POME treatment.     

Biodegradation of 4-nitrophenol in a two-phase sequencing batch reactor: concept demonstration,kinetics and modelling

The objectives of this work were to demonstrate the potential of a two-phase sequencing batch reactor in degrading xenobiotics and to evaluate the kinetic parameters leading to a mathematical model of the system. 4-Nitrophenol (4NP), a typical representative of substituted phenols, was selected as the target xenobiotic; this compound has never been remediated in a two-phase bioreactor before. Partition tests were conducted to determine the most appropriate partitioning solvent, and among the three investigated solvents (1-undecanol, 2-undecanone and oleyl alcohol), 2-undecanone was chosen because of its favourable partition coefficient and its negligible emulsion-forming tendencies. Moreover, the selected solvent showed satisfactory biocompatibility characteristics with respect to the biomass, with only minor effects on the intrinsic microbial kinetics. Kinetic tests were then performed in a sequencing batch reactor (2-l volume) operated in both conventional one- and two-phase configurations, with the two-phase system showing a significant improvement in the process kinetics in terms of reduced inhibition and increased maximum removal rate. The obtained kinetic parameters suggest that the two-phase sequencing batch system may find full-scale application, as the maximum removal rate k _max (~3 mg 4NP mgVSS⁻¹ day⁻¹) is of the same order of magnitude of heterotrophic bacteria operating in wastewater treatment plants.     

Laccase activity from the fungus Trametes hirsuta using an air-lift bioreactor

AIM: To produce high laccase activities from the white-rot fungus Trametes hirsuta in an in-house air-lift bioreactor (ALB). METHODS AND RESULTS: Trametes hirsuta was grown in a 6-l ALB. A fed-batch strategy with glycerol as an addition resulted in maximum laccase activity of 19,400 U l(-1), which was the highest reported from the fungus. CONCLUSION: The ALB configuration with additional glycerol resulted in high laccase activities. SIGNIFICANCE AND IMPACT OF THE STUDY: This study provides useful information on how to produce high concentrations of laccase.     

Biodegradability of extracellular polymeric substances produced by aerobic granules

This study investigated the biodegradability of extracellular polymeric substances (EPS) produced by aerobic granules. Aerobic granules were precultivated with synthetic wastewater in a lab-scale sequencing batch reactor. EPS were extracted from aerobic granules and were then fed as the sole carbon source to their own producers. Results showed that about 50% of EPS produced by aerobic granules could be utilized by their producers under aerobic starvation condition. The average biodegradation rate of the granule EPS in terms of chemical oxygen demand was five times slower than that of acetate, but 50 times faster than that of nonbiodegradable EPS produced by aerobic granules. The nonbiodegradable EPS was mainly found on the outer shell of aerobic granule. EPS produced by aerobic granules basically comprised two major components, i.e., biodegradable and nonbiodegradable EPS. The biodegradable EPS could serve as a useful energy source to sustain the growth of aerobic granules under starvation. This study provides experimental evidence that part of the EPS produced by aerobic granules would be biodegradable, but only nonbiodegradable EPS would play a crucial role in maintaining the structural integrity of aerobic granule.     

Aerobic granulation under the combined hydraulic and loading selection pressures

Two SBR reactors were set up to investigate the feasibility of aerobic granulation under the combined selection pressures of hydraulic shear force and substrate loading. Aerobic granulation was studied at superficial upflow air velocity of 3.2 and 2.4 cm/s under an organic loading rate (OLR) range of 6.0-15.0 kg COD/m3d. Good reactor performance and well granule characteristics were achieved in a wide OLR range from 6.0 high up to 15.0 kg COD/m3d at 3.2 cm/s. While under the velocity of 2.4 cm/s, stable operation was limited in the OLR range of 6.0-9.0 kg COD/m3d and failed to operate with granule deterioration under further higher OLRs. The optimal combination of hydrodynamic shear force and loading selection pressure was demonstrated to be an important factor that influence aerobic granulation and govern the granule characteristics and reactor performance.     

气提式内循环硝化反应器运行性能的研究

气提式内循环反应器具有很好的生物硝化性能,能承受高进水氨浓度（78.49mmol/L）,具有高容积转化效率（163.18 mmol/L·d）,运行性能稳定（氨去除率保持在94.42%以上）。在气提式内循环反应器的运行过程中,可产生硝化颗粒污泥。颗粒污泥开始出现的时间约为45d,颗粒污泥的粒径平均值0.83 mm,沉降速度55.53m/h,氨氧化活性0.95mmol (NH⁺₄-N)/g(VS)·d。硝化颗粒污泥也具有厌氧氨氧化活性,氨氧化速率0.23mmol (NH⁺₄-N)/g(VS)·d,亚硝酸还原速率0.24mmol (NO^-₂-N)/g(VS)·d。     

Biodegradation of methyl <Emphasis Type="Italic">t</Emphasis>-butyl ether by aerobic granules under a cosubstrate condition

Aerobic granules efficient at degrading methyl tert-butyl ether (MTBE) with ethanol as a cosubstrate were successfully developed in a well-mixed sequencing batch reactor (SBR). Aerobic granules were first observed about 100 days after reactor startup. Treatment efficiency of MTBE in the reactor during stable operation exceeded 99.9%, and effluent MTBE was in the range of 15–50 μg/L. The specific MTBE degradation rate was observed to increase with increasing MTBE initial concentration from 25 to 500 mg/L, which peaked at 22.7 mg MTBE/g (volatile suspended solids)·h and declined with further increases in MTBE concentration as substrate inhibition effects became significant. Microbial-community deoxyribonucleic acid profiling was carried out using denaturing gradient gel electrophoresis of polymerase chain reaction-amplified 16S ribosomal ribonucleic acid. The reactor was found to be inhabited by several diverse bacterial species, most notably microorganisms related to the genera Sphingomonas, Methylobacterium, and Hyphomicrobium vulgare. These organisms were previously reported to be associated with MTBE biodegradation. A majority of the bands in the reactor represented a group of organisms belonging to the Flavobacteria–Proteobacteria–Actinobacteridae class of bacteria. This study demonstrates that MTBE can be effectively degraded by aerobic granules under a cosubstrate condition and gives insight into the microorganisms potentially involved in the process.     

Amylase activity in substrate deficiency aerobic granules

Immunohistochemical staining was applied together with the multicolor fluorescent scheme to demonstrate the amylase activity for polysaccharide hydrolysis in stored or starved aerobic granules that are in substrate deficiency. If sufficient nutrients were present, α-amylase and β-amylase were found close to the surface layer of the original granules. Following storage or starvation during which most external nutrients were depleted, the α-amylase and β-amylase were distributed over the entire granule interior, suggesting endogenous respiration at the core of the granule. In particular, the fluorescent intensities of α-amylase and β-amylase were enriched 5–20 μm from the edge of the internal cavity, suggesting the strong correlation between polysaccharide hydrolysis and the formation of interior cavities. The secreted amylase was located near the living cells, suggesting that the polysaccharide hydrolysis is restricted to local environment that occurs near the functional strains. Internal hydrolysis within the core, for the case of both proteins and polysaccharides should correspond in principle to the loss of granule stability.     

Characteristics and stability of aerobic granules cultivated with different starvation time

The characteristics of aerobic granules at steady state and the effects of starvation time on the stability of aerobic granules during the long-term operation were investigated in three sequencing batch reactors (SBRs R1–R3). The SBRs were operated with a cycle time of 1.5, 4.0, and 8.0 h, respectively, which resulted in a starvation time of 0.8, 3.3, and 7.3 h in three reactors, respectively. Results showed that aerobic granules were successfully cultivated in the three reactors, but the granules in R2 with a starvation time of 3.3 h showed the highest density and the best settleability at steady state. It is obvious that the starvation time has an optimum value in terms of settleability of granules. In addition, it was found that the coexistence of a minority of fluffy granules with smooth granules was the potential unstable factor in R1 with a starvation time of 0.8 h at the steady state. The sudden dominance of fluffy granules in R1 after the 160-day operation led to the operation failure of the reactor R1, whereas the granules in R2 with a starvation time of 3.3 h and R3 with a starvation time of 7.3 h showed good stability during the long-term operation. As short starvation time leads to the instability of granules, and long starvation time is not advisable for practical application due to low efficiency, starvation time should be controlled in a reasonable range.     

生物造粒流化床污水处理反应器中微生物的分布特征

对生物造粒流化床污水处理反应器10cm、60cm、110cm处好氧细菌总数以及反硝化菌、反硫化菌分别进行计数,同时,用光学显微镜、扫描电子显微镜以及石蜡切片技术对粒状污泥中细菌的分布情况进行研究。结果发现,流化床中好氧细菌非常丰富,在反应器10cm处,每克污泥微生物的数量可达1.6×10⁸个,说明好氧细菌在生物造粒流化床有机物生物降解中起主导作用;同时,流化床中也有一定数量的兼性厌氧菌存在,并且随着流化床床体的升高有增加的趋势,这与溶解氧(DO)随流化床床体高度的增加而迅速降低有关;随着回流比的增加,溶解氧增高,相应的好氧细菌有所增加而兼性厌氧菌减少;对于颗粒污泥,其表面和内部微生物分布数量有很大的差异。     

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.     

Effects of the internal recycling rate on biological nutrient removal and microbial community structure in a sequential anoxic/anaerobic membrane bioreactor

This study investigated the effects of the internal recycling rate on nutrients removal in a sequential anoxic/anaerobic membrane bioreactor (SAM). Microbial community structure in sludge from the SAM was studied using quinone profile method. Above 98% COD, 68% nitrogen, and 55% phosphorus removal efficiencies were achieved when the internal recycling rate was 2.5 times influent flow. At that rate, the optimum specific nitrate loading rate and COD/NO(3)-N ratio were found to be 2.24 mgNO(3)-N g(-1) MLSS h(-1) and 9.13, respectively. Batch tests demonstrated that anoxic condition suppressed phosphorus release, and that denitrification was also influenced by initial substrate concentration. Denitrification appeared to have some priority over phosphorus release for substrate uptake. Microbial community analysis revealed a predominance of the subclass beta-Proteobacteria. Furthermore, it was found that Rhodocyclus-related bacteria were efficient at phosphorus removal than Actinobacteria.     

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.     

Is sludge retention time a decisive factor for aerobic granulation in SBR?

This study investigated the role of sludge retention time (SRT) in aerobic granulation under negligible hydraulic selection pressure. Results showed that no successful aerobic granulation was observed at the studied SRTs in the range of 3-40 days. A comparison analysis revealed that hydraulic selection pressure in terms of the minimum settling velocity would be much more effective than SRT for enhancing heterotrophic aerobic granulation in sequencing batch reactor (SBR). It was shown that SRT would not be a decisive factor for aerobic granulation in SBR.