Reactivation of biocatalysts after long-term storage and startup of the DEAMOX process

Studies of our laboratory have led to elaboration of the DEAMOX (DEnitrifying AMmonia OXidation) technology intended for removal of nitrogen contaminants from wastewater. The DEAMOX process comprises two anaerobic stages implemented by the same sludge biocatalyst, namely, denitratation (conversion of nitrate to nitrite) and anammox reaction (ANaerobic AMmonium nitrogen OXidation by nitrite). The results of reactivation of biocatalysts after their long-term storage (5 and 16 months) and successful startup of the DEAMOX process in two modifications (S- and O-) are described. An S-DEAMOX process was launched using a sludge biocatalyst with restored anammox activity of 20.1 mg N/g VSS/day; this process provided removal of 78% of nitrogen in reactor over 20 days. The launched O-DEAMOX process with the sludge biocatalyst with anammox activity of 6.1 mg N/g VSS/day provided for 87% removal of the total nitrogen compounds over 30 days. Two different electron donors were used at the stage of nitrate conversion to nitrite, namely, an inorganic donor, sulfide (S-DEAMOX), and an organic one, acetate (O-DEAMOX).     

Combined removal of sulfur compounds and nitrate by autotrophic denitrification in bioaugmented activated sludge system

An autotrophic denitrification process using reduced sulfur compounds (thiosulfate and sulfide) as electron donor in an activated sludge system is proposed as an efficient and cost effective alternative to conventional heterotrophic denitrification for inorganic (or with low C/N ratio) wastewaters and for simultaneous removal of sulfide or thiosulfate and nitrate. A suspended culture of sulfur-utilizing denitrifying bacteria was fast and efficiently established by bio-augmentation of activated sludge with Thiobacillus denitrificans. The stoichiometry of the process and the key factors, i.e. N/S ratio, that enable combined sulfide and nitrogen removal, were determined. An optimum N/S ratio of 1 (100% nitrate removal without nitrite formation and low thiosulfate concentrations in the effluent) has been obtained during reactor operation with thiosulfate at a nitrate loading rate (NLR) of 17.18 mmol N L(-1) d(-1). Complete nitrate and sulfide removal was achieved during reactor operation with sulfide at a NLR of 7.96 mmol N L(-1) d(-1) and at N/S ratio between 0.8 and 0.9, with oxidation of sulfide to sulfate. Complete nitrate removal while working at nitrate limiting conditions could be achieved by sulfide oxidation with low amounts of oxygen present in the influent, which kept the sulfide concentration below inhibitory levels.     

ANAMMOX process start up and stabilization with an anaerobic seed in Anaerobic Membrane Bioreactor (AnMBR)

ANaerobic AMMonium OXidation (ANAMMOX) process, an advanced biological nitrogen removal alternative to traditional nitrification--denitrification removes ammonia using nitrite as the electron acceptor without oxygen. The feasibility of enriching anammox bacteria from anaerobic seed culture to start up an Anaerobic Membrane Bioreactor (AnMBR) for N-removal is reported in this paper. The Anammox activity was established in the AnMBR with anaerobic digester seed culture from a Sewage Treatment Plant in batch mode with recirculation followed by semi continuous process and continuous modes of operation. The AnMBR performance under varying Nitrogen Loading Rates (NLR) and HRTs is reported for a year, in terms of nitrogen transformations to ammoniacal nitrogen, nitrite and nitrate along with hydrazine and hydroxylamine. Interestingly ANAMMOX process was evident from simultaneous Amm-N and nitrite reduction, consistent nitrate production, hydrazine and hydroxylamine presence, notable organic load reduction and bicarbonate consumption.     

亚硝酸盐对污水生物除磷影响的研究进展

亚硝酸盐作为生物硝化和反硝化的中间产物, 存在于污水生物脱氮除磷系统中。对于生物强化除磷工艺亚硝酸盐既是电子受体用于反硝化除磷, 同时又是抑制剂影响生物除磷过程。本文综述了聚磷菌在厌氧、好氧和缺氧环境中的代谢机理, 在此基础上分别从好氧除磷和反硝化除磷两方面介绍了亚硝酸盐对污水生物除磷影响的研究, 同时概述了亚硝酸盐对生物除磷的抑制机理, 并对该领域的研究提出了个人见解。     

新型固定化硝化细菌和好氧反硝化细菌处理氨氮废水

以改性沸石、聚乙烯醇、海藻酸钠作为固定化载体材料,硼酸和氯化钙作为交联剂,采用吸附-包埋-交联法将硝化细菌和好氧反硝化细菌复合固定化制备成微生物小球.通过复合菌配比实验,考察其对氨氮的去除率以及亚硝酸盐和硝酸盐的累积量;对制成的固定化小球做四因素三水平的正交实验,考察不同条件下对氨氮的去除率.结果表明,硝化细菌和好氧反硝化细菌配比为3:2时,氨氮去除率最高达82.32%,亚硝酸盐和硝酸盐的累积量为0.032mg·L^-1和0.053 mg·L^-1;通过正交实验,确定沸石投加量为2g·100mL^-1、温度为30℃、pH值为7.5、振荡速度为130r·min^-1时,对氨氮达到最好的去除效果,去除率达90.31%,此法制得的小球机械性能和吸水性能良好.     

Batch culture enrichment of ANAMMOX populations from anaerobic and aerobic seed cultures

Discharge of nitrate and ammonia rich wastewaters into the natural waters encourage eutrophication, and contribute to aquatic toxicity. Anaerobic ammonium oxidation process (ANAMMOX) is a novel biological nitrogen removal alternative to nitrification-denitrification, that removes ammonia using nitrite as the electron acceptor. The feasibility of enriching the ANAMMOX bacteria from the anaerobic digester sludge of a biomethanation plant treating vegetable waste and aerobic sludge from an activated sludge process treating domestic sewage is reported in this paper. ANAMMOX bacterial activity was monitored and established in terms of nitrogen transformations to ammonia, nitrite and nitrate along with formation of hydrazine and hydroxylamine.     

Nitrogen removal from polluted river by enhanced floating bed grown canna

Floating beds of canna can remove nitrogen from polluted river water, but the removal efficiency is not very high in a short time, so some enhanced methods must be used to improve nitrogen removal efficiency by the system. Immobilized denitrifying bacteria and aeration were added into the canna floating bed. The experimental results showed that these enhancements substantially improved the nitrogen removal efficiency of the floating beds. With the enhancements, total nitrogen removal was 72.1%, ammonia nitrogen oxidation was 100%, nitrate nitrogen removal was 75.8%, nitrite nitrogen removal was 95.9%, and COD removal was 94.6% in 5 days. Without the enhancements, the canna floating bed system removed only 50.4% of the total nitrogen, 22.4% of the nitrate nitrogen, 5.3% of the nitrite nitrogen and 39.9% of the COD, respectively, in 5 days, but did accomplish 100% oxidation of the ammonia nitrogen. The experimental results provide an improved method for the treatment of polluted river water.     

Evaluation of Anammox and denitrification during anaerobic digestion of poultry manure

Two approaches based on ne w process development and biological nitrogen transformation were investigated in a bench study for removing nitrogen as N2 gas from poultry waste while stabilizing the wastes. The process, known as "Anammox", was explored in batch anaerobic culture using serum bottles. The Anammox process involves the use of nitrite as an electron acceptor in the bacterially mediated oxidation of ammonia to yield N2. Studies are described wherein nitrite was added to poultry waste and the effects on ammonium levels were monitored. About 13-22% ammonium removal was observed with the inoculation of returned activated sludge, and the total ammonium reduction was not proportional to the reduction of nitrite, thereby suggesting that Anammox was less competitive under the conditions in our studies. The addition of nitrite and nitrate was not inhibitory to the process based on gas generation and COD reduction. The classical nitrogen removal process of nitrification followed with denitrification offers a more reliable basis for nitrogen removal from poultry wastes.     

Impact of protozoan grazing on nitrification and the ammonia- and nitrite-oxidizing bacterial communities in activated sludge

In activated sludge, protozoa feed on free-swimming bacteria and suspended particles, inducing flocculation and increasing the turnover rate of nutrients. In this study, the effect of protozoan grazing on nitrification rates under various conditions in municipal activated sludge batch reactors was examined, as was the spatial distribution of ammonia-oxidizing bacteria (AOB) and nitrite-oxidizing bacteria (NOB) within the activated sludge. The reactors were monitored for ammonia, nitrite, nitrate, and total nitrogen concentrations, and bacterial numbers in the presence and absence of cycloheximide (a protozoan inhibitor), allylthiourea (an inhibitor of ammonia oxidation), and EDTA (a deflocculating agent). The accumulations of nitrate, nitrite, and ammonia were lower in batches without than with protozoa grazing. Inhibition of ammonia oxidation also decreased the amount of nitrite and nitrate accumulation. Inhibiting protozoan grazing along with ammonia oxidation further decreased the amounts of nitrite and nitrate accumulated. Induction of deflocculation led to high nitrate accumulation, indicating high levels of nitrification; this effect was lessened in the absence of protozoan grazing. Using fluorescent in situ hybridization and confocal laser scanning microscopy, AOB and NOB were found clustered within the floc, and inhibiting the protozoa, inhibiting ammonia oxidation, or inducing flocculation did not appear to lower the number of AOB and NOB present or affect their position within the floc. These results suggest that the AOB and NOB are present but less active in the absence of protozoa.     

Recent developments on biological nutrient removal processes for wastewater treatment

The need for preserving the environment is tightening regulations limiting the discharge of contaminants into water bodies. Nowadays most of the effort is done on the removal of more specific contaminants such as nutrients (N and P) and sulfurous compounds since they are becoming of great concern due to its impact on the quality of water bodies. There have been two recent discoveries of microbial conversions of nitrogenous compounds. One consisting on the capability of ammonia oxidizers of denitrify under certain conditions resulting in a new one-step method for the removal of N-compounds. The second has been named the ANAMMOX process, wherein ammonium is oxidized to dinitrogen gas with nitrite as the electron acceptor. Other developments consist of operational strategies aiming at obtaining the highest efficiency at removing nitrogen at lowest cost. One strategy consists of the partial nitrification to nitrite (only successful in the SHARON process) and subsequently either the heterotrophic denitrification of nitrites or its autotrophic reduction by ANAMMOX microorganisms. Another strategy consists of the coexistence of nitrifiers and denitrifiers in the same reactor by implementing high frequency oscillations on the oxygen level.The recent developments on biological phosphorous removal are based on the capacity of some denitrifying microorganisms to store ortho-phosphate intracellular as poly-phosphate in the presence of nitrate. These microorganisms store substrate (PHB) anaerobically which is further oxidized when nitrate is present. By extracting excess sludge from the anoxic phase, phosphate is removed from the system. Removing phosphate using nitrate instead of oxygen has the advantage of saving energy (oxygen input) and using less organic carbon.The microbial conversions of sulfurous compounds involve the metabolism of several different specific groups of bacteria such as sulfate reducing bacteria, sulfur and sulfide oxidizing bacteria, and phototrophic sulfur bacteria. Some of these microorganisms can simultaneously use nitrate, what has been reported as autotrophic denitrification by sulfur and sulfide oxidizing microorganisms. More recently, the anaerobic treatment of an industrial wastewater rich in organic matter, nitrogen and sulfate, reported a singular evolution of N and S compounds that initially was hypothesized as SURAMOX (SUlfate Reduction and AMmonia OXidation). The process could not have been verified nor reproduced and further investigations on the proposed SURAMOX mechanism have given no additional insights to those initial observations.     

Mixed culture of nitrifying bacteria and denitrifying bacteria for simultaneous nitrification and denitrification

A mixed culture containing nitrifying bacteria and denitrifying bacteria was investigated for aerobic simultaneous nitrification and denitrification. A mixture of NaHCO₃ and CH₃COONa was selected as the appropriate carbon source for cell growth and nitrogen removal, the concentrations of carbon and nitrogen sources were also examined. Ammonia could be oxidized aerobically to nitrite by the mixed culture, and the intermediate nitrite was then reduced to dinitrogen gas. No nitrite was detected during the process. 0.212 g of ammonia/l could be removed in 30 h and nitrate could not be utilized aerobically by the mixed culture. Nitrite could be degraded aerobically as well as anaerobically. Very little ammonia was degraded anaerobically, but the ability to degrade ammonia could be recovered even after oxygen had been supplied for 42 h.     

The performance and microbial communities of biodegradation-electron transfer with sulfur metabolism integrated process for flue gas desulfurization wastewater treatment

The biodegradation-electron transfer with sulfur metabolism integrated (BESI®) process was used for the treatment of real flue gas desulfurization wastewater. The BESI® process consists of an anaerobic activated sludge reactor, an anoxic activated sludge reactor, and an aerobic bio-film reactor. The performance of the integrated process was evaluated by the removal efficiencies of organics and nitrogen pollutants. The sulfate in the wastewater was used as an abundant sulfur source to drive the integrated process. The removal efficiencies of chemical oxygen demand, total organic carbon, ammonia nitrogen, and total nitrogen of the integrated process were 87.99, 87.04, 30.77, and 45.17%, respectively. High-throughput 454-pyrosequencing was applied for the analysis of microbial communities in the integrated process. From the anaerobic activated sludge (Sample 1), anoxic activated sludge (Sample 2), and aerobic bio-film (Sample 3), totals of 1701, 1181, and 857 operational taxonomic units were obtained, respectively. The sulfur cycle was associated with the removal of organics and nitrogen pollutants. The sulfate-reducing bacteria participated in the organics removal in the anaerobic reactor, and the sulfide oxidation was related with the denitrification in the anoxic reactor. A complete nitrogen degradation chain was built in the integrated process. Through the degradation chain, the nitrogenous organic pollutants, ammonia nitrogen, and nitrate could be removed. The participant functional bacteria were also detected by pyrosequencing.     

Enhanced biological nutrient removal using MUCT-MBR system

Biological nutrient removal was investigated in a combined modified University of Cape Town and membrane bioreactor system. When the influent nutrient mass ratio (COD/TN/TP) was 28.5/5.1/1 to 28.5/7.2/1, average removal efficiencies of COD, TN and TP were 90%, 81.6%, 75.2%. Obvious denitrifying phosphorus removal occurred with C/N ratio 3.98. When nitrite was the main electron acceptor, the ratio of denitrifying phosphate uptake to the total phosphate uptake were 99.8% and the sludge yield was 0.28kg VSS/kg COD; when nitrate was the main electron acceptor, the ratio was 92% and the yield was 0.32kg VSS/kg COD. In case of nitrite, the system not only kept TP and TN removal at 89.1% and 82.2%, but also ensured less sludge production. Batch tests showed that the proportion of denitrifying phosphorus-accumulating organisms in the total phosphorus-accumulating organisms in the system was higher than 80%.     

Selenite reduction by a denitrifying culture: batch- and packed-bed reactor studies

Selenite reduction by a bacterial consortium enriched from an oil refinery waste sludge was studied under denitrifying conditions using acetate as the electron donor. Fed-batch studies with nitrate as the primary electron acceptor showed that accumulation of nitrite led to a decrease in the extent of selenite reduction. Also, when nitrite was added as the primary electron acceptor, rapid selenite reduction was observed only after nitrite was significantly depleted from the medium. These results indicate that selenite reduction was inhibited at high nitrite concentrations. In addition to batch experiments, continuous-flow selenite reduction experiments were performed in packed-bed columns using immobilized enrichment cultures. These experiments were carried out in three phases: in phase I, a continuous nitrate feed with different inlet selenite concentration was applied; in phase II, nitrate was fed in a pulsed fashion; and in phase III, nitrate was fed in a continuous mode but at much lower concentrations than the other two phases. During the phase I experiments, little selenite was removed from the influent. However, when the column was operated in the pulse feed strategy (phase II) or in the continuous mode with low nitrate levels (phase III), significant quantities of selenium were removed from solution and retained in the immobilization matrix in the column. Thus, immobilized denitrifying cultures can be effective in removing selenium from waste streams, but nitrate-limited operating conditions might be required.     

Nitrogen removal from wastewaters at low C/N ratios with ammonium and acetate as electron donors

A denitrifying upflow anaerobic sludge blanket (UASB) reactor was operated at different nitrate loading rates at a C/N ratio of 1.2, with acetate as an electron donor. This resulted in an increase in the accumulation of nitrite. After this, the UASB reactor was supplemented with 100 mg NH4+-Nl(-1) d(-1), while acetate was gradually limited in the medium. This prevented nitrite accumulation at a C/N ratio of 0.6 due to an enhanced nitrite reduction rate achieved in the reactor. An increasing amount of ammonium was consumed when the C/N ratio was lowered in the medium. This suggested that ammonium was used as an alternative electron donor during denitrification, which is supported by nitrogen balances. Nitrite was shown to be toxic for the nitrogen removal process at 200-400 mg NO2--N(l(-1) when the C/N ratio was decreased to 0.4 leading to formation of ammonium. The present study showed that addition of ammonium as an alternative electron donor for denitrification achieved a nitrogen removal process with negligible accumulation of undesirable intermediates.     

一株高效去除亚硝酸氮细菌的分离鉴定及其脱氮特性研究

【目的】从南美白对虾养殖塘中分离到高效去除亚硝酸氮的细菌, 对其分类和脱氮特性进行了研究。【方法】 以除亚硝酸氮为主要指标, 取养殖塘底层水样分离筛选菌株; 依据16S rRNA基因序列和生理生化特征初步鉴定菌株; 研究不同碳源、碳氮比、起始pH、温度、摇床转速和氯化钠浓度对反硝化除亚硝酸氮的影响, 并考查了菌株对硝酸氮和氨氮的利用情况。【结果】得到的菌株中菌株FP6活性最高, 初步鉴定菌株FP6属于地衣芽孢杆菌。菌株FP6的生长最适脱氮碳源为蔗糖, 菌株FP6去除亚硝酸氮有高活性的条件范围为: C/N值15?25、起始pH 7.0?10.0、温度20 °C?37 °C、摇床转速0?200 r/min和氯化钠浓度0?40 g/L。菌株FP6对硝酸氮和氨氮都有一定的去除能力, 利用硝酸氮时不积累亚硝酸氮。【结论】地衣芽孢杆菌FP6具有优良的除亚硝氮特性, 适宜的温度、pH和盐度范围较宽。     

Kinetic limitations during the simultaneous removal of <Emphasis Type="Italic">p</Emphasis>-cresol and sulfide in a denitrifying process

The aim of this study was to evaluate the capacity of a denitrifying consortium to achieve the simultaneous removal of nitrate, sulfide and p-cresol and elucidate the rate-limiting steps in the mixotrophic process. Nitrite reduction appeared as the most evident rate-limiting step in the denitrifying respiratory process. The nitrite reduction rate achieved was up to 57 times lower than the nitrate reduction rate during the simultaneous removal of sulfide and p-cresol. Negligible accumulation of N₂O occurred in the denitrifying cultures corroborating that nitrite reduction was the main rate-limiting step of the respiratory process. A synergistic effect of nitrate and sulfide is proposed to explain the accumulation of nitrite. The study also points at the oxidation of S⁰ as another rate-limiting step in the denitrifying process. Different respiratory rates were achieved with the distinct electron donors provided (p-cresol and sulfide). The oxidation rate of p-cresol (q_CRES) was generally higher (up to 2.6-fold in terms of reducing equivalents) than the sulfide oxidation rate (q_S2−), except for the experiments performed at 100 mg S²⁻ L⁻¹ in which q_S2− was slightly (~1.4-fold in terms of reducing equivalents) higher than q_CRES. The present study provides kinetic information, which should be considered when designing and operating denitrifying reactors to treat industrial wastewaters containing large amounts of sulfurous, nitrogenous and phenolic contaminants such as those generated from petrochemical refineries.     

Fully coupled activated sludge model (FCASM): Model development

A sub-microscopic mechanism model named Fully Coupled Activated Sludge Model (FCASM) about biological nutrient removal in the wastewater treatment process was developed in the present study. The functional organisms existing simultaneously in the activated sludge system were separated into eight groups, including aerobic heterotrophic organisms, nitrite reducing organisms, nitrate reducing organisms, ammonium oxidizing autotrophs, nitrite oxidizing autotrophs, non-denitrifying phosphorus-accumulating organisms (PAOs), denitrifying phosphorus-accumulating bacteria (DPB), and glycogen-accumulating organisms (GAOs). In FCASM, the interaction relationships of the eight functional microorganisms were taken fully into account. FCASM could model biological nitrogen removal via nitrite by splitting nitrification process and denitrification process into two-step reactions, and the autotrophs and denitrifying organisms were divided into two groups, respectively. What’s important, FCASM included the anaerobic maintenance processes of sequential utilization of polyphosphate followed by glycogen for PAOs and DPB and glycolysis of the intracellular stored glycogen for GAOs.     

利用硝酸盐和亚硝酸盐同步富集厌氧甲烷氧化微生物的比较实验

【背景】反硝化厌氧甲烷氧化(Denitrifying anaerobic methane oxidation,DAMO)是以硝酸盐或亚硝酸盐为电子受体以甲烷为电子供体的厌氧氧化过程,对认识全球碳氮循环、削减温室气体排放和开发废水脱氮新技术等方面具有重要意义。【目的】认识以硝酸盐和亚硝酸盐为电子受体的DAMO微生物富集过程和结果的差异性。【方法】在序批式反应器(Sequencing batch reaetor,SBR)内接种混合物,分别以硝酸盐和亚硝酸盐为电子受体连续培养800 d,定期检测反应器基质浓度变化、计算转化速率;利用16S rRNA基因系统发育分析研究功能微生物的多样性,利用实时荧光定量PCR技术定量测定功能微生物。【结果】以亚硝酸盐为电子受体的1、3号反应器富集到了DAMO细菌,未检测到DAMO古菌;以硝酸盐为电子受体的2号反应器富集到了DAMO细菌和古菌的混合物;3个反应器的脱氮速率经过初始低速期、快速提升期,最终达到稳定,但2号快速提升期开始时间比1、3号晚了80 d左右,达到稳定的时间更长,稳定最大速率为1、3号的44.7%、40.3%。【结论】硝酸盐和亚硝酸盐对富集产物有决定性影响;以硝酸盐为电子受体富集得到的DAMO古菌和细菌协同体系可以长期稳定共存,DAMO古菌可能是协同体系中脱氮速率的限制性因素。     

Rapid start-up and performance of denitrifying granular sludge in an upflow sludge blanket (USB) reactor treating high concentration nitrite wastewater

Denitrifying granular sludge reactor holds better nitrogen removal efficiency than other kinds of denitrifying reactors, while this reactor commonly needs seeding anaerobic granular sludge and longer period for start-up in practice, which restricted the application of denitrifying granular sludge reactor. This study presented a rapid and stable start-up method for denitrifying granular sludge. An upflow sludge blanket (USB) reactor with packings was established with flocculent activated sludge for treatment of high concentration nitrite wastewater. Results showed mature denitrifying granular sludge appeared only after 15 days with highest nitrogen removal rate of 5.844 kg N/(m³ day), which was much higher than that of compared anoxic sequencing batch reactor (ASBR). No significant nitrite inhibition occurred in USB and denitrification performance was mainly influenced by hydraulic retention time, influent C/N ratio and internal reflux ratio. Hydraulic shear force created by upflow fluid, shearing of gaseous products and stable microorganisms adhesion on the packings might be the reasons for rapid achievement of granular sludge. Compared to inoculated sludge and ASBR, remarkable microbial communitiy variations were detected in USB. The dominance of Proteobacteria and Bacteroidetes and enrichment of species Pseudomonas_stutzeri should be responsible for the excellent denitrification performance, which further verified the feasibility of start-up method.