氯苯对EGSB反应器内颗粒污泥性质影响的研究*

采用EGSB反应器处理含氯苯有机废水 ,主要研究了氯苯对颗粒污泥性质的影响。结果表明 :氯苯对处理葡萄糖自配水的EGSB反应器内颗粒污泥中的细菌有较强毒害作用 ,连续投加低浓度氯苯 72d后 ,扫描电镜观察可发现颗粒污泥表面和内部细菌均明显受到损害 ,停止投加氯苯恢复运行 30d和 5 0d后 ,仍可观察到颗粒污泥内部细菌受损害的现象 ,且部分颗粒污泥内部存在着明显的空洞 ;随着运行时间的延长 ,反应器内颗粒污泥的粒径有较大程度的增大 ;但长期接触氯苯导致部分颗粒污泥解体 ,使得小粒径污泥增多 ,而大粒径     

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。     

球形红细菌污泥颗粒化及降解氯苯

投加絮凝剂是促使微生物快速形成污泥颗粒的一种有效手段,通过研究在不同絮凝剂下生成的生物絮体的形态和沉降性能,推荐选用聚合氯化铝(PAC)作为促进光合细菌球形红细菌形成污泥颗粒的絮凝剂。PAC的最佳投加量范围为140-160mg/L,其中,PAC投加量150mg/L时,促进污泥颗粒化的效果最好。考察球形红细菌污泥颗粒降解氯苯的环境条件,结果表明球形红细菌污泥颗粒降解氯苯的最佳条件为好氧、pH7.0、30°C。     

酸性条件下耐酸产甲烷颗粒污泥的培养及特性*

分别采用中性颗粒污泥和河底沉积物接种运行两个颗粒污泥膨胀床(EGSB)反应器,通过逐级降低pH的运行策略,驯化和培养了耐酸产甲烷颗粒污泥,两个EGSB反应器均能在pH5．8-6．2条件下稳定运行,容积负荷可达5．5-7．5kg COD,(m^3／d),COD去除率约90％;两种颗粒污泥在低pH值下均能保持较高的产甲烷活性,pH5．5时,仍能保持pH7．0时活性的51．8％和55．6％;还对耐酸颗粒污泥的粒径分布、沉降性能、金属元素含量、微观结构及细菌在颗粒表面和内部的分布等进行了研究。     

五氯酚在污染沉积物泥浆固液两相中厌氧生物降解

研究了污染沉积物泥浆液、固两相五氯酚(PCP)厌氧生物降解.结果表明,投加10g·kg^-1厌氧颗粒污泥,经31d处理泥浆液、固两相PCP降解率达98.9%,平均降解速率达到80mg·kg^-1·d^-1,对照处理平均降解速率仅为4.4mg·kg^-1·d^-1,颗粒污泥生物强化作用明显.作为泥浆修复过程的调控因子,有机溶剂、共基质和表面活性剂对PCP降解效应不同,投加乙醇,可提高PCP解吸和降解速率,4d内两相PCP降解速率达到54.3mg·kg^-1·d^-1;而投加共基质和非离子表面活性剂乙二醇丁醚后,液、固两相PCP降解均出现迟滞,两者均不同程度地抑制PCP降解.     

成熟厌氧颗粒污泥的结构及其特征*

厌氧序批式反应器〈AnaerobicSequencingBatchReactorASBR〉在处理啤酒废水过程中 ,能形成厌氧颗粒污泥。文中采用扫描电子显微镜和荧光显微镜技术对成熟厌氧颗粒污泥的结构及微生物群落等进行跟踪观察 ,结果显示 ,颗粒污泥结构复杂 ,细菌以微群落形式分布 ,其中产甲烷菌占一定比例。同时也探讨了厌氧颗粒污泥的形成机制。     

五氯酚（PCP）污染土壤厌氧生物修复技术的初步研究

研究土壤泥浆反应器在投加厌氧颗粒污泥条件下修复PCP污染土壤的性能.结果表明,对PCP浓度30mg     

中试厌氧氨氧化反应器的启动与调控

研究了中试厌氧氨氧化(Anaerobic ammonium oxidation,Anammox)反应器的启动性能。结果表明,以硝化反硝化污泥、短程硝化污泥、厌氧絮体污泥和厌氧颗粒污泥混合接种,经过255d的运行,可在常温下(5oC～27oC)成功启动中试Anammox反应器,反应器的基质氮去除速率可达1.30kg/(m3·d)。厌氧氨氧化是致碱反应,厌氧氨氧化成为反应器内的主导反应后,进水pH宜控制在厌氧氨氧化适宜范围的偏低水平(6.8左右)。亚硝酸盐既是Anammox菌的基质,也是抑制剂,控制进水亚硝酸盐浓度(13～36mg/L)有助于厌氧氨氧化反应。菌种是生物反应器的功能之源,向中试装置投加少量厌氧氨氧化污泥(投加比2%),可大大加速中试Anammox反应器的启动进程。     

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。     

厌氧氨氧化膨胀床反应器的运行性能

试验研究了以竹炭为载体的厌氧氨氧化膨胀床反应器的运行性能.接种反硝化污泥,用模拟废水可成功启动该反应器:运行至144 d时,容积总氮去除率达到3.02 kg N/m3/d.这是国内文献报道的最高水平.动力学分析表明.这种反应器的最大容积总氮去除率可迭12.77 kg N/m3/d.具有很大的脱氮潜能.反应器的启动过程可分为菌体自溶、活性延滞和活性提高三个阶段.与此相应,污泥性状也从黄褐色絮状污泥变为棕灰色颗粒污泥和红色颗粒污泥.红色颗粒污泥以杆茵和球菌为主.厌氧氨氧化活性可达0.56mg TN/(mgprotein)/h,它们是反应器厌氧氨氧化功能的主要承载者.     

Anammox反应器启动过程中颗粒污泥性状变化特性

以厌氧颗粒污泥作为接种物,通过185 d的运行,成功启动了上流式厌氧氨氧化污泥床(Upflow anaerobic sludge blanket,UASB)反应器。反应器的进水氨氮与亚硝氮浓度分别提升至224 mg/L和255 mg/L,容积氮去除速率提升至3.76 kg/(m3·d)。采用红外光谱、扫描电镜和透射电镜等对厌氧氨氧化颗粒污泥的性状进行观察,发现颗粒污泥在启动过程中经历了污泥颗粒裂解到污泥颗粒重组的过程,且厌氧氨氧化颗粒污泥表面含有丰富的官能团,说明厌氧氨氧化颗粒污泥可能具有良好的吸附性能。采用宏基因组测序的方法对启动前后颗粒污泥的生态结构进行分析,发现原接种污泥优势菌群(变形菌门、厚壁菌门、拟杆菌门)丰度大幅减少,厌氧氨氧化菌所属的浮霉状菌门丰度则由1.59%提升到23.24%。     

Challenge of psychrophilic anaerobic wastewater treatment

Psychrophilic anaerobic treatment is an attractive option for wastewaters that are discharged at moderate to low temperature. The expanded granular sludge bed (EGSB) reactor has been shown to be a feasible system for anaerobic treatment of mainly soluble and pre-acidified wastewater at temperatures of 5--10 degrees C. An organic loading rate (OLR) of 10--12 kg chemical oxygen demand (COD) per cubic meter reactor per day can be achieved at 10--12 degrees C with a removal efficiency of 90%. Further improvement might be obtained by a two-module system in series. Stabile methanogenesis was observed at temperatures as low as 4--5 degrees C. The specific activity of the mesophilic granular sludge was improved under psychrophilic conditions, which indicates that there was growth and enrichment of methanogens and acetogens in the anaerobic system. Anaerobic sewage treatment is a real challenge in moderate climates because sewage belongs to the 'complex' wastewater category and contains a high fraction of particulate COD. A two-step system consisting of either an anaerobic up-flow sludge bed (UASB) reactor combined with an EGSB reactor or an anaerobic filter (AF) combined with an anaerobic hybrid reactor (AH) is successful for anaerobic treatment of sewage at 13 degrees C with a total COD removal efficiency of 50% and 70%, respectively.     

Granular sludge formation in upflow anaerobic sludge blanket (UASB) reactors

The state of the art for upflow anaerobic sludge blanket (UASB) reactors is discussed, focusing on the microbiology of immobilized anaerobic bacteria and the mechanism of granule formation. The development of granular sludge is the key factor for successful operation of the UASB reactors. Criteria for determining if granular sludge has developed in a UASB reactor is given based on the densities and diameters of the granular sludge. The shape and composition of granular sludge can vary significantly. Granules typically have a spherical form with a diameter from 0.14 to 5 mm. The inorganic mineral content varies from 10 to 90% of the dry weight of the granules, depending on the wastewater composition etc. The main components of the ash are calcium, potassium, and iron. The extracellular polymers in the granular sludge are important for the structure and maintenance of granules, while the inorganic composition seems to be of less importance. The extracellular polymer content varies between 0.6 and 20% of the volatile suspended solids and consists mainly of protein and polysaccharides. Both Methanosaeta spp. (formerly Methanothrix) and Methanosarcina spp. have been identified as important aceticlastic methanogens for the initial granulation and development of granular sludge. Immunological methods have been used to identify other methanogens in the granules. The results have showed that, besides the aceticlastic methanogens Methanosaeta spp. and Methanosarcina spp., hydrogen and formate utilizing bacteria are also present, e.g., Methanobacterium formicicum, Methanobacterium thermoautotrophicum, and Methanobrevibacter spp. Microcolonies of syntrophic bacteria are often observed in the granules, and the significant electron transfer in these microcolonies occurs through interspecies hydrogen transfer. The internal organization of the various groups of bacteria in the granules depends on the wastewater composition and the dominating metabolic pathways in the granules. Internal organization is observed in granules where such an arrangement is beneficial for an optimal degradation of the wastewater. A four-step model is given for the initial development of granular sludge. (c) 1996 John Wiley & Sons, Inc.     

Development of anaerobic sludge bed (ASB) reactor technologies for domestic wastewater treatment: motives and perspectives

During the treatment of raw domestic wastewater in the upflow anaerobic sludge blanket (UASB) reactor, the suspended solids (SS) present in the wastewater tend to influence negatively the methanogenic activity and the chemical oxygen demand (COD) conversion efficiency. These problems led to the emergence of various anaerobic sludge bed systems such as the expanded granular sludge bed (EGSB), the upflow anaerobic sludge blanket (UASB)-septic tank, the hydrolysis upflow sludge bed (HUSB), the two-stage reactor and the anaerobic hybrid (AH) reactor. However, these systems have, like the UASB reactor, limited performance with regard to complete treatment (e.g., removal of pathogens). In this respect, a new integrated approach for the anaerobic treatment of domestic wastewater is suggested. This approach combines a UASB reactor and a conventional completely stirred tank reactor (CSTR) for the treatment of the wastewater low in SS and sedimented primary sludge, respectively. The principal advantages of the proposed system are energy recovery from organic waste in an environmentally friendly way; lowering the negative effect of suspended solids in the UASB reactor; production of a high quality effluent for irrigation; and prevention of odour problems.     

Biosorption and biodegradation of pentachlorophenol (PCP) in an upflow anaerobic sludge blanket (UASB) reactor

In order to understand the fate of PCP in upflow anaerobic sludge blanket reactor (UASB) more completely, the sorption and biodegradation of pentachlorophenol (PCP) by anaerobic sludge granules were investigated. The anaerobic granular sludge degrading PCP was formed in UASB reactor, which was seeded with anaerobic sludge acclimated by chlorophenols. At the hydraulic retention time (HRT) of 20–22 h, and PCP loading rate of 200–220 mg l⁻¹ d⁻¹, UASB reactor exhibited good performance in treating wastewater which containing 170–180 mg l⁻¹ PCP and the PCP removal rate of 99.5% was achieved. Sequential appearance of tetra-, tri-, di-, and mono-chlorophenol was observed in the reactor effluent after 20 mg l⁻¹ PCP introduction. Sorption and desorption of PCP on the anaerobic sludge granules were all fitted to the Freundlich isotherm equation. Sorption of PCP was partly irreversible. The Freundlich equation could describe the behavior of PCP amount sorbed by granular sludge in anaerobic reactor reasonably well. The results demonstrated that the main mechanism leading to removal of PCP on anaerobic granular sludge was biodegradation, not sorption or volatization.     

Introduction of ade novo bioremediation activity into anaerobic granular sludge using the dechlorinating bacterium DCB-2

The strictly anaerobic, pentachlorophenol (PCP) degrading bacterium DCB-2 was immobilized in an Upflow Anaerobic Sludge Blanket (UASB) reactor containing sterile granules. PCP and lactate were fed to the reactor and the concentration of chlorophenols in the effluent were monitored for 641 days. PCP was found to be degraded and transformed into 3.4.5-trichlorophenol in the reactor where DCB-2 was introduced into the granular sludge. PCP was still transformed to 3.4.5-trichlorophenol when the hydraulic retention time was decreased to six hours which was much lower than the generation time of DCB-2 insuring no free living cells in the reactor. This indicated that DCB-2 was immobilized in the granular layer. A control reactor that contained only sterile granules did not dechlorinate PCP indicating that the performance in the inoculated reactor was only due to the introduced bacteria. Immobilization of DCB-2 in the granules was further demonstrated by adding an antibody raised against DCB-2 to sliced granules. Bacteria thus visualized formed a net structure inside the granules. No DCB-2 bacteria could be found in granules from the control reactor. When lactate was omitted from the influent, the reactor still dechlorinated PCP in accordance with our findings that lactate was not used by DCB-2. This suggested that the reducing equivalents for reductive dechlorination were derived from the granules themselves. The reactor performance was 120 mol·l reactor^-1·day^-1, comparable to the best described performance of a UASB-reactor and to aerobic reactors. Our study demonstrates that granules can be constructed which possess specific abilities such as a dechlorinating activity and at the same time be high performing. This result have implications for eco-engineering of granules for anaerobic treatment of contaminated waters.     

Methanogenesis in an Upflow Anaerobic Sludge Blanket Reactor at pH 6 on an Acetate-Propionate Mixture

High-rate anaerobic digestion can be applied in upflow anaerobic sludge blanket reactors for the treatment of various wastewaters. In upflow anaerobic sludge blanket reactors, sludge retention time is increased by a natural immobilization mechanism (viz. the formation of a granular type of sludge). When this sludge is cultivated on acid-containing wastewater, the granules mainly consist of an acetoclastic methanogen resembling Methanothrix soehngenii. This organism grows either in rods or in long filaments. Attempts to cultivate a stable sludge consisting predominantly of Methanosarcina sp. on an acetate-propionate mixture as substrate by lowering the pH from 7.5 during the start-up to approximately 6 failed. After 140 days of continuous operation of the reactor a filamentous organism resembling Methanothrix soehngenii prevailed in the sludge. The specific methanogenic activity of this sludge on acetate-propionate was optimal at pH 6.6 to 6.8 and 7.0 to 7.2, respectively.     

Simultaneous biological removal of sulfur, nitrogen and carbon using EGSB reactor

High-rate biological conversion of sulfide and nitrate in synthetic wastewater to, respectively, elemental sulfur (S⁰) and nitrogen-containing gas (such as N₂) was achieved in an expanded granular sludge bed (EGSB) reactor. A novel strategy was adopted to first cultivate mature granules using anaerobic sludge as seed sludge in sulfate-laden medium. The cultivated granules were then incubated in sulfide-laden medium to acclimate autotrophic denitrifiers. The incubated granules converted sulfide, nitrate, and acetate simultaneously in the same EGSB reactor to S⁰, N-containing gases and CO₂ at loading rates of 3.0 kg S m⁻³ d⁻¹, 1.45 kg N m⁻³ d⁻¹, and 2.77 kg Ac m⁻¹ d⁻¹, respectively, and was not inhibited by sulfide concentrations up to 800 mg l⁻¹. Effects of the C/N ratio on granule performance were identified. The granules cultivated in the sulfide-laden medium have Pseudomonas spp. and Azoarcus sp. presenting the heterotrophs and autotrophs that co-work in the high-rate EGSB-SDD (simultaneous desulfurization and denitrification) reactor.     

Effect of ethylene glycol-bis(β-aminoethyl ether)-N,N-tetraacetic acid (EGTA) on stability and activity of methanogenic granular sludge

Summary The effect of the calcium-specific chelant ethylene glycol-bis(\-aminoethyl ether)-N,N-tetraacetic acid (EGTA) on methanogenic granular sludge from a laboratory-scale upflow anaerobic sludge-blanket (UASB) reactor fed propionate and from a full-scale reactor treating paper-mill waste-water was studied. Upon treatment with EGTA both sludge types showed a decrease in the calcium and phosphorus content and a release of protein and polysaccharides, leading to a decrease in strength of papermill granular sludge and a disintegration of propionate-grown granules. After treatment of propionate-grown granular sludge with high EGTA concentrations, the methanogenic activity with propionate and acetate as test substrates decreased by 88 and 33%, respectively. The marked reduction in propionate oxidation activity may be caused by a disruption of the special juxtapositioning of bacteria in the granules. Offsprint requests to: A. J. B. Zehnder     

Anaerobic granule development for removal of pentachlorophenol in an upflow anaerobic sludge blanket (UASB) reactor

The granulation process using synthetic wastewater containing pentachlorophenol (PCP) in four 1.1 l laboratory scale upflow anaerobic sludge blanket (UASB) reactors was studied, and the anaerobic biotransformation of PCP during the granulation process investigated. After 110 days granular sludge was developed and up to 160 and 180 mg/l of PCP was added into the reactors R1 and R2, respectively, when they were inoculated with acclimated anaerobic sludge from an anaerobic digester of a citric acid plant. The inoculum was predominately composed of bacilli and filamentous bacteria. Granulation did not occur in reactors R3 and R4 which were inoculated with acclimated anaerobic sludge from aerobic sludge of the municipal sewage treatment plant which consisted mainly of cocci. Despite similar bacilli in the granule, the filamentous bacteria from reactor R1 were thicker than those of reactor R2. The granular sludge had a maximum diameter of 2.5 and 2.2 mm, and SMA of 1.44 and 1.32 gCOD/gTVS per day for reactors R1 and R2, respectively. Over 98% chemical oxygen demand (COD) removal rate and 99% of PCP removal rate were achieved when reactors R1 and R2 were operated at PCP and COD loading rates of 150 and 7.5 g/l per day, respectively. H₂-producing acetogens were the dominant anaerobes in the granular sludge.