长期饥饿后SPNA微颗粒污泥系统性能恢复

为了确定长期饥饿后连续流一段式部分亚硝化-厌氧氨氧化（SPNA）工艺的性能恢复情况,采用连续流反应器,考察了在室温下（11~23℃）经历161d饥饿期的SPNA系统性能恢复策略的可行性及脱氮性能和菌群结构变化.通过控制DO浓度及进水氨氮负荷,逐渐实现亚硝酸盐氧化菌（NOB）的抑制和淘汰、氨氧化菌（AOB）和厌氧氨氧化菌（AnAOB）的活性恢复和富集.在68d内系统总氮去除率恢复至72.13%,氨氮去除率恢复至94.75%.微颗粒污泥（³200μm）的占比从42.04%升至60.98%.微生物群落结构分析发现,停止运行161d后系统Candidatus Kuenenia的相对丰度升至25.53%,表现出较强的抵抗饥饿条件的能力,系统恢复后其相对丰度逐渐降低,接近反应器饥饿前水平.AOB的高底物利用能力是系统恢复的前提,AnAOB活性的提高是系统恢复的关键.系统性能的成功恢复表明室温下161d饥饿期对系统造成的影响是可逆的,长期室温下储存SPNA污泥是可行的.     

CRI系统厌氧氨氧化协同反硝化脱氮的启动及性能

为进一步提高脱氮效率,该文采用人工快渗(CRJ)系统作为厌氧氨氧化反应器,考察了有机物添加对氮素污染物转化及菌群结构的影响,探讨了厌氧氨氧化协同反硝化脱氮的可行性.结果 表明,通过逐步提高进水COD浓度至20 mg/L,可在49d内实现CRI系统厌氧氨氧化协同反硝化的快速启动,稳定运行期间TN平均去除率达到98.1％,相比未添加有机物时启动周期缩短了11d,TN平均去除率提高了7.3％.当进水COD浓度提高至25 mg/L时,厌氧氨氧化对脱氮的贡献率降低了27.2％,主要厌氧氨氧化功能菌属Candidatus Kuenenia的相对丰度降至12.42％,而反硝化功能菌属Flavobacterium的相对丰度升至11.16％,反硝化菌与厌氧氨氧化菌竞争反应基质而导致厌氧氨氧化活性被削弱,TN平均去除率下降了13.5％.因此,将进水有机物浓度控制在适宜范围时可有效改善厌氧氨氧化的脱氮性能.     

厌氧氨氧化颗粒污泥快速培养及其抑制动力学

为实现厌氧氨氧化颗粒污泥(ANAMMOX granular sludge,AGS)的快速培养,采用上流式厌氧污泥床(up-flow anaerobic sludge bed,UASB)工艺,在添加少量絮状厌氧氨氧化污泥(flocculent ANAMMOX sludge,FAS)的反应器内填充生物流离球作为填料,对ANAMMOX的启动及FAS的颗粒化进行研究.同时利用Haldane模型研究AGS的基质抑制动力学特性.结果表明,利用生物流离球作为填料,实现了ANAMMOX的启动,总氮去除率达85%以上,总氮容积负荷为0. 72 kg·(m3·d)-1,并在127 d内成功培养出直径1. 0～3. 0 mm的AGS.动力学研究表明,反应器内AGS对氨和亚硝酸盐的最大反应速率分别为1. 46 kg·(kg·d)-1和1. 76 kg·(kg·d)-1,半抑制速率分别是852. 2 mmol·L-1和108. 2 mmol·L-1.与絮状污泥相比,AGS能承受更高的氨和亚硝酸盐抑制浓度,并保持较高的反应速率.采用含有海绵的生物流离球作为填料,能有效加速反应器的启动,加快AGS的形成,对厌氧氨氧化工艺的实际运行具有积极的意义.     

基于SBR反应器的ANAMMOX工艺的启动运行

采用SBR反应器,接种好氧硝化污泥,在142 d内于较高负荷下成功启动了厌氧氨氧化反应器.反应器总氮容积负荷(以N计)为0.43 kg/m3·d,总氮去除率最高达到93.3%,平均为80.5%;氨氮和亚硝酸盐氮的去除率最高达到93.9%和99.8%,平均去除率为81.2%和85.7%.在稳定运行阶段,氨氮去除量、亚硝酸盐氮去除量、硝酸盐氮生成量三者之间的比值为1:1.38:0.18.反应器启动过程中,出水、进水pH差值的变化趋势由负到正,然后稳定在一定范围内;且污泥性状有较大变化,污泥中微生物所占比率有所提高,整个反应器中适应厌氧氨氧化运行方式的菌种增殖较快.     

Quantity and activity of ammonia-oxidizing archaea and bacteria and their contribution to ammonia oxidation in farmland soil of Qinghai-Tibet Plateau北大核心CSCD

Ammonia oxidation, the first and rate-limiting step of nitrification, is mainly performed by ammonia-oxidizing archaea (AOA) and ammonia-oxidizing bacteria (AOB). However, the activities of AOA and AOB in soil and their relative contribution to ammonia oxidation are unclear, and whether there is a significant correlation between the quantity of AOA and AOB and the ammonia oxidation rate is also controversial. In this study, quantitative PCR combined with acetylene (C2H2) and 1-octyne inhibition methods were used to determine the quantity and activity of AOA and AOB in wheat, highland barley, and oilseed rape soils in Nyingchi, Lhatse, Sangzhuzi, and Sangri counties on the Qinghai-Tibet Plateau. The results showed that the quantity of AOB ((2.34 ± 0.84) ×105 - (2.65 ± 1.07) ×106 copies g-1 dry soil) was significantly higher than that of AOA ((0.20 ± 0.10) ×104 - (4.02 ± 0.39) ×104 copies g-1 dry soil) in all the soil samples. Soil pH was the key factor affecting the quantity of AOB, and the total phosphorus and ammonium nitrogen in soil were the key factors affecting the quantity of AOA. The rates of ammonia oxidation in the farmland soils of Lhatse (2.42 ± 0.73 mg kg-1 d-1) and Sangzhuzi (3.24 ± 1.15 mg kg-1 d-1) were significantly higher than those in the soils of Nyingchi (1.17 ± 0.43 mg kg-1 d-1) and Sangri counties (0.88 ± 0.57 mg kg-1 d-1). The rates of ammonia oxidation in the farmland soils of Lhatse and Sangzhuzi were dominated by AOB, while those in the farmland soils of Nyingchi and Sangri counties were dominated by AOA. For crops, the ammonia oxidation rates of wheat and oilseed rape soils in all four regions were significantly higher than those of highland barley soil, whereas the activity of AOA and AOB was not influenced by crops. The ratio of nitrogen to phosphorus was the key factor influencing AOA activity, whereas soil pH and total carbon were the main factors influencing AOB activity. Additionally, the quantities of AOA and AOB were not significantly correlated with the total ammonia oxidation rates and AOA and AOB activity. Overall, our study suggests that both AOA and AOB play important roles in ammonia oxidation in farmland soils of the Qinghai-Tibet Plateau. Moreover, it is unreliable to predict the activity of AOA and AOB and their relative contribution to ammonia oxidation directly based on their number of amoA genes, and the activity of AOA and AOB should be directly and accurately measured. These results are important for understanding ammonia nitrogen removal processes, slowing nitrate loss, and reducing the emission of the greenhouse gas nitrous oxide in the farmland ecosystem of the Qinghai-Tibet Plateau. © 2022 Science Press. All rights reserved.     

生物可降解地膜覆盖对关中地区小麦-玉米农田温室气体排放的影响

为探究生物可降解地膜覆盖对冬小麦-夏玉米轮作农田生态系统温室气体排放的影响,布设了普通地膜覆盖（PM）、生物可降解地膜覆盖（BPM）和无覆盖（CK）这3个处理,采用静态暗箱-气相色谱仪法监测了2018～2019年土壤CO₂、 CH₄和N₂O的排放通量,并用水分利用效率（WUE）、温室气体排放强度（GHGI）和净生态系统经济预算（NEEB）指标评估覆膜对作物产量、农田环境和经济效益的影响.结果表明,与CK相比,PM和BPM增加了玉米季土壤CO₂的排放,PM处理下CO₂排放总量高于BPM处理（P>0.05）.PM和BPM处理均能够显著减少土壤对CH₄的吸收,CH₄的年吸收量较CK处理分别减少了42.0%和24.2%（P<0.05）.与CK相比,PM和BPM增加了小麦季N₂O排放总量（P>0.05）,而显著降低了夏玉米季N₂O排放（P<0.05）.覆膜能够提高作物产量和水分...     

不同接种物启动Anammox 反应器的性能研究

采用上流式生物膜滤器(UBF)研究了以厌氧颗粒污泥和反硝化污泥作为接种物启动厌氧氨氧化(Anammox)反应器的性能.结果表明,2 种接种物均能成功启动Anammox 反应器.启动过程可分为菌体自溶阶段、活性迟滞阶段、活性提高阶段和活性稳定阶段.这种启动过程的阶段性特征符合Logistic 方程.以厌氧颗粒污泥启动Anammox 反应器,菌体自溶阶段较长(49d),活性迟滞阶段较短(8d),基质去除速率最高可达2090mg/(L·d);以反硝化污泥启动Anammox 反应器,菌体自溶阶段较短(3d),而活性迟滞阶段较长(36d),基质去除速率最高可达1030mg/(L·d).分别以负荷提升前后的基质去除速率、基质去除率以及出水基质浓度的变化情况作为效能指标评价2 个反应器运行的稳定性,以厌氧颗粒污泥作为接种物启动Anammox 反应器的稳定性能明显占优势.在高负荷率下运行,以反硝化污泥作为接种物启动的Anammox 反应器较易失稳.根据启动过程的阶段性和反应器运行的稳定性,对Anammox 反应器采取相应的调控对策可促进启动过程的顺利进行.     

SH-A工艺处理焦化污水的工业应用

通过对丹东焦化有限公司污水处理站工艺流程改造前后的处理效果、动力消耗及运行稳定性等进行分析对比,证明采用改造后的SH-A新工艺处理焦化污水脱氮率高、运行费用低,处理后出水达到《污水综合排放标准》(GB8978-1996)一级,可回用于熄焦。该工艺适合应用于焦化行业的污水处理。     

温度变化对不同污泥形态厌氧氨氧化菌活性的影响

以Ca.Brocadia为主要种属的厌氧氨氧化颗粒污泥和生物膜为研究对象,通过测定不同温度下厌氧氨氧反应活化能以探讨温度对以不同污泥形态存在的厌氧氨氧化菌的短期影响.结果表明,在15～25℃和25～35℃,以颗粒污泥及生物膜形态存在的厌氧氨氧化菌的反应活化能不同.在15～25℃,颗粒污泥和生物膜中的厌氧氨氧化反应活化能...     

氨法脱硫技术在烧结烟气治理领域应用研究

LS氨法烟气脱硫技术是一种在传统基础上进行改进的湿法烟气脱硫技术。以66 m2烧结机烟气治理方案为例,分析LS氨法烟气脱硫技术各项技术指标,同时对该方法脱硫技术特点、经济运行进行全面分析。通过论述得出结论,LS氨法烟气脱硫技术是一种适合于冶金行业烧结机烟气治理的一项湿法技术。