多级AO耦合流离生化工艺流量分配比优化及脱氮机制

为探究进水流量分配比对低温城市污水脱氮效率的影响,并解析多级AO耦合流离生化工艺脱氮规律,实验采用三级AO耦合流离生化工艺,在温度为(10±1)℃、水力停留时间8 h、气水比恒定的条件下处理模拟低C/N值城市污水.系统依次在进水比5∶4∶4(等容积负荷)、3∶2∶1(等停留时间)和25∶15∶6(等污泥负荷)这3种工况下运行.结果表明,该工艺对低温低C/N值污水的处理效果较好,其中在进水比为3∶2∶1的工况下脱氮效率最高,COD、NH+4-N和TN平均去除率分别为87. 44%、96. 63%和76. 81%.进一步对氮的迁移转化规律进行研究发现,制约工艺低温脱氮的主要因素为各级硝化效率,3∶2∶1的进水比合理地分配了进水负荷,各级硝化率均超过85%,为反硝化创造了有利条件,最终获得了较高的脱氮效率,此时系统也具有最高的总生物量.研究结果丰富了多级AO耦合工艺低温脱氮理论,同时为工程设计应用提供参考.     

污泥超高温堆肥过程中DOM结构的光谱分析

为了明确超高温堆肥新工艺在促进腐殖化进程中的优势,采用三维荧光光谱(3D-EEM)等光谱学方法研究了污泥超高温堆肥过程中DOM的结构特征及其变化规律.结果表明,堆体≥80℃的超高温阶段持续5 d(最高温度90℃),50℃以上高温阶段达到22 d,反映了堆肥过程中强烈的微生物代谢活性.E253/E203、SUVA280、S275~295等9个紫外-可见光光谱(UV-Vis)指标在0~23 d变化显著,指出DOM的芳香化和堆肥腐殖化程度逐渐增强.3D-EEM光谱结合荧光区域体积积分技术(FRI)分析指出,DOM中蛋白类物质在超高温堆肥过程的0~6 d几乎完全被降解;腐殖酸和富里酸类物质在0~23 d大量形成,堆肥在高温阶段达到完全腐熟,这与种子发芽指数(GI)在23 d所指示的腐熟度评价结果(98.5%)一致.基于多种光谱学指标的相关性分析,PⅤ,n/PⅢ,n与其它光谱学均呈现较好的相关性(r≥0.68),可以作为评价超高温堆肥腐熟度的光谱学指标.上述结果证实了超高温堆肥工艺可加快堆肥腐熟进程、缩短堆肥周期至20 d左右,在有机固废资源化领域具有极大的应用潜力.     

四环素抗生素对污泥中四环素抗性基因丰度和表达水平的作用影响

为研究四环素(TC)抗生素对其抗性基因(TC-ARGs)转录表达的作用影响,以从活性污泥中筛选获得的四环素抗性细菌(TRB)作为研究对象,采用荧光定量PCR和逆转录PCR方法检测了7种TC-ARGs,包括tet A、tet C、tet G、tet M、tet O、tet W和tet X基因的丰度和表达水平,并探讨了TC与TC-ARGs丰度及其表达水平之间的相关关系.结果表明,在整个培养周期内,tet A、tet G和tet W基因丰度随TC暴露浓度的增大总体呈现上升趋势,但其余TC-ARGs基因丰度整体波动较大. TC胁迫对不同TC-ARGs的转录表达水平作用影响差别较大,其中,tet A基因表达水平相对稳定,且随TC浓度的升高而上调,在TC浓度为100 mg·L^-1时,其上调倍数高达5. 3倍.在短期(1 d) TC胁迫下,TC-ARGs转录表达水平随TC浓度的升高整体呈现上调趋势.由相关性分析可知,tet A和tet W基因丰度与其转录表达水平之间存在显著的线性相关性,表明其基因丰度可在一定程度上衡量和评价其抗性表达水平,进而反映其功能活性和环境风险.     

Insights into the mechanism of the deterioration of mainstream partial nitritation/anammox under low residual ammonium

Residual ammonium is a critical parameter affecting the stability of mainstream partial nitritation/anammox (PN/A), but the underlying mechanism remains unclear. In this study, mainstream PN/A was established and operated with progressively decreasing residual ammonium. PN/A deteriorated as the residual ammonium decreased to below 5 mg/L, and this was paralleled by a significant loss in anammox activity in situ and an increasing nitrite oxidation rate. Further analysis revealed that the low-ammonium condition directly decreased anammox activity in situ via two distinct mechanisms. First, anammox bacteria were located in the inner layer of the granular sludge, and thus were disadvantageous when competing for ammonium with ammonium-oxidizing bacteria (AOB) in the outer layer. Second, the complete ammonia oxidizer (comammox) was enriched at low residual ammonium concentrations because of its high ammonium affinity. Both AOB and comammox presented kinetic advantages over anammox bacteria. At high residual ammonium concentrations, nitrite-oxidizing bacteria (NOB) were effectively suppressed, even when their maximum activity was high due to competition for nitrite with anammox bacteria. At low residual ammonium concentrations, the decrease in anammox activity in situ led to an increase in nitrite availability for nitrite oxidation, facilitating the activation of NOB despite the dissolved oxygen limitation (0.15–0.35 mg/L) for NOB persisting throughout the operation. Therefore, the deterioration of mainstream PN/A at low residual ammonium was primarily triggered by a decline in anammox activity in situ. This study provides novel insights into the optimized design of mainstream PN/As in engineering applications.     

Test of membrane bioreactor for waste water treatment in a petrochemical complex

Membrane bioreactor (MBR) used in water and waste water treatment is a developing technique for water pollution control and water reuse. This paper describes a membrane-bioreactor for treatment of waste water in a petrochemical complex. The experimental MBR was a lab scale one composed of an activated sludge bioreactor unit and an ultrafiltration membrane unit. The relationship of COD removal with MLSS and HRT in this MBR was studied. The effects of crossflow velocity, backwash interval and volume of flush liquid on the flux were discussed. The results showed that average removal of COD, oil, SS and turbidity in petrochemical waste water by the MBR was 91%, 86%, 92% and 99% respectively. The average removal of NH₃-N and total phosphorous was 85% and 82%. A coefficient of COD removal, k, was 0.017-0.080 L/(mg.d). The membrane flux maintained higher than 60 L/hm2 bar for 34 days without chemical cleaning when the velocity of crossflow was 3.5-3.9 m/s and the backwash interval was 30 minutes and backwash duration at 20 seconds. The results indicated that it is feasible for MBR technology to be used in petrochemical waste water treatment. The treated water could be considered as a source used to make up water for industrial cooling system or to be reused for other purposes.     

无剩余污泥接触氧化法处理漂染废水的探讨

对漂染废水的处理，虽能做到达标排放，但其剩余污泥的生成量也过多，该文以上海信泰纺织品有限公司无剩余污泥接触氧化法处理漂染废水的实例，表明了既可提高污染物去除率，又能节省投资和运转费用，通过两年的运行实践，证明效果良好，在对酸化反应器的设计和有效控制方面，以及氧化反应器与酸化反应器的运行管理等方面也进行了探讨。     

用呼吸仪监测取代酚类化合物对活性污泥的抑制

应用呼吸仪测定活性污泥中微生物的活性。研究了九种取代酚对微生物活性的影响,发现抑制效应与有机物的正辛醇-水分配系数、最低未占轨道能级有着相关联系,并发现取代酚对活性污泥硝化细菌比起异养细菌有着更强的抑制。生物膜比活性污泥具有更好的耐抑制能力,驯化对抗抑制有明显的效果,增大污泥浓度在一定程度上可以减轻毒害。     

污泥厌氧消化预处理技术综述

全球环境问题已成为国际社会关注的焦点,围绕全球气候变化,降低温室气体排放,寻求再生能源,节能减排已成为目前国际科技发展的方向。通过"十一五"污水处理厂的建设,每年污泥产量已接近3000万吨(含水率80%脱水污泥计)以上,且以每年10%的速度递增。其处理与处置是制约社会经济发展的重要问题。但是,城市污泥蕴含有大量生物质能,通过借鉴国外先进技术与经验,开发城市污泥生物质能提取和利用技术,对我国节能减排具有重要战略意义。由于细胞壁的存在,使得污泥水解成为限制厌氧消化效率的重要瓶颈,而污泥强化预处理可有效提高污泥细胞壁的破坏,溶出胞内有机物,最大化回收剩余污泥中的有机能源。目前,预处理技术较多,如超声波预处理、热处理、微波预处理、碱解处理、臭氧预处理等,本文从物理、化学等角度分析了不同预处理对厌氧消化技术的影响。     

超声波去除农用污泥中重金属的试验研究

污水处理厂污泥中的重金属浓度高是污泥农用的主要障碍。为了降低农用污泥中的重金属含量,以Cu、Zn、Ni、Pb为对象,研究了超声波对其的影响。结果表明:超声对污泥中重金属有一定的溶出作用。当超声时间为30min时,溶解状态Cu、Zn、Ni、Pb的析出率分别为42.1%、37.5%、12.7%、14.7%;总的析出率分别为52.7%、44.7%、23.6%、71%。其中析出的Pb大部分以胶体状态存在,而溶解状态只占很少一部分。其他几种金属则以溶解状态为主。     

CaCl2盐度对活性污泥性能影响的研究

针对某企业高含盐有机生产废水,采用传统活性污泥法,实验研究了氯化钙盐度对活性污泥性能的影响,分别研究了盐度对有机物的去除能力、活性污泥中微生物的耗氧速率、活性污泥的结构和沉淀效果及对菌胶团中微生物生态的影响。结果表明,当氯化钙盐度从0mg/L升高到40000mg/L的时候,废水中COD的去除率由92.9%降低到56%,活性污泥的耗氧速率下降,菌胶团的微生物种类也随之减少,MLVSS/MLSS下降,活性污泥中的无机成分增加,沉淀性能增强,菌胶团也更为致密。