碳酸盐-硫酸盐矿物强化垃圾渗滤液厌氧处理研究

厌氧消化通常是垃圾渗滤液生物处理的首要环节,但处理效率不高.本研究尝试通过添加碳酸盐、硫酸盐等矿物来提高垃圾渗滤液的厌氧转化效率.研究共设置5组厌氧生物反应器,包括投加硬石膏、方解石、石膏、白云石的反应器及空白对照,考察添加矿物对垃圾渗滤液厌氧消化的影响.从实验结果可以看出,添加矿物的反应器中COD的去除率可以达到75%左右,而空白对照组去除率尚不足60%,添加矿物反应器甲烷产量显著高于对照.从反应器中的p H变化可以看出,矿物的添加可以提高溶液中的p H.研究结果表明,添加碳酸盐/硫酸盐矿物对垃圾渗滤液中的有机物厌氧消化过程具有重要的促进作用.     

处理水产养殖污水潜流湿地中的厌氧氨氧化菌群特征

厌氧氨氧化(anaerobic ammonium oxidation,ANAMMOX)是潜流湿地净化污水的重要功能,目前关于潜流湿地厌氧氨氧化特征还不清楚.为了解处理水产养殖污水潜流湿地中的厌氧氨氧化特点,采用16S rRNA基因克隆文库和实时荧光定量PCR技术以及多样性分析等方法,对处理水产养殖污水潜流湿地中ANAMMOX菌的结构、多样性和丰度进行了研究分析.结果表明,处理水产养殖污水潜流湿地中存在Candidatus brocadia和Candidatus kuenenia这2类已知的ANAMMOX菌和3类未知的ANAMMOX菌,其优势种群为Candidatus brocadia;在不同季节中,秋季潜流湿地中ANAMMOX菌的多样性最高(H',1.21),春季最低(H',0.64);在养殖周期内,潜流湿地中ANAMMOX菌的丰度(以鲜重计,下同)在8.0×104~9.4×106copies·g-1之间,总细菌丰度在7.3×109~9.1×1010copies·g-1之间;在潜流湿地不同层面以及不同季节中,ANAMMOX菌的丰度存在着明显的差异,总细菌丰度则差异不明显,ANAMMOX菌的丰度在不同层面上的差异没有随时间变化的规律性.根据潜流湿地中ANAMMOX菌的分布特征,改变养殖污水布水方式和调整湿地结构可以提高潜流湿地的反硝化效果.该研究为进一步优化潜流湿地结构,提高净化养殖污水效率提供了依据.     

Innovative combined technique for high concentration of azo dye AR18 wastewater treatment using modified SBR and enhanced Fenton process as post treatment

The purpose of this research was to evaluate the performance of combined biological/advanced oxidation process (AOP) system for treatment of wastewater containing high concentration (500 mg/L) of azo dye Acid Red 18 (AR18). Two alternating anaerobic–aerobic sequencing batch reactors (SBR1 and SBR2 without and with external feeding at the beginning of aeration cycle, respectively) were operated. The effluent of the SBRs was then post treated through enhanced Fenton process (using zero-valent iron combined with ultrasonic irradiation). More than 90% and 97% of COD was removed in the combined SBR/AOP system without external carbon source (CTS1) and with external feeding (CTS2), respectively. The analysis of dye and its metabolites using UV–vis and HPLC analysis also proved that 99% of the original dye was decolorized and more than 89% of its metabolites were degraded through CST2 which is significantly higher than the reported values in the literature. Besides, more than 87% of phosphorus removal efficiency was obtained in CST2 compared to only 54.5% removal efficiency in CST1. Regarding the findings of this study, the proposed combined treatment system (CTS2) can be suggested as an effective technique for treatment of high azo dye AR18 concentration wastewater.     

ABR+生物接触氧化法处理高浓度有毒有机废水

本文采用ABR+生物接触氧化组合工艺处理含苯酚的高COD有毒有机废水,实验研究了ABR反应器的抗毒性及对COD、苯酚和NH3-N的处理效果。实验结果表明:废水COD和苯酚的去除主要发生在厌氧阶段;在苯酚质量浓度1 000 mg/L左右时,ABR反应器和常规厌氧反应器的处理效率均出现明显的下降趋势,但ABR反应器对苯酚的耐受浓度明显高于常规厌氧反应器;相比于常规厌氧反应器,ABR反应器推流式的特性实现了产酸和产甲烷优势菌群的分离,具有较高的COD、苯酚的去除率和较强的抗毒性;对NH3-N的去除,ABR反应器的强化效果不明显。     

多溴联苯醚微生物降解过程与机理的研究进展

多溴联苯醚(PBDEs)属溴代阻燃剂,曾因其优良的阻燃性能而广泛应用于电子电器、石油化工和建材纺织等工业产品中.然而,随着大量生产和使用,PBDEs已成为大气、水体、土壤和生物体等多环境介质中普遍检出且极具生态风险的有机污染物.因此,开展微生物降解研究对于典型环境中PBDEs污染风险消除和污染修复,具有重要的科学意义.本文从PBDEs环境归趋行为及其暴露风险出发,综述了PBDEs微生物厌氧降解和好氧降解的最新研究动态,比较分析了两种降解过程的降解特性与影响因素,并针对微生物,尤其是好氧微生物降解机理,阐述了bph A或etb A功能基因及其编码酶对PBDEs好氧降解过程的调控作用,同时就PBDEs微生物高效降解菌种选育、降解机理等方面的研究趋势进行了展望.     

Determination of the archaeal and bacterial communities in two-phase and single-stage anaerobic systems by 454 pyrosequencing

2-Phase anaerobic digestion (AD), where the acidogenic phase was operated at 2 day hydraulic retention time (HRT) and the methanogenic phase at 10 days HRT, had been evaluated to determine if it could provide higher organic reduction and methane production than the conventional single-stage AD (also operated at 12 days HRT). 454 pyrosequencing was performed to determine and compare the microbial communities. The acidogenic reactor of the 2-phase system yielded a unique bacterial community of the lowest richness and diversity, while bacterial profiles of the methanogenic reactor closely followed the single-stage reactor. All reactors were predominated by hydrogenotrophic methanogens, mainly Methanolinea. Unusually, the acidogenic reactor contributed up to 24% of total methane production in the 2-phase system. This could be explained by the presence of Methanosarcina and Methanobrevibacter, and their activities could also help regulate reactor alkalinity during high loading conditions through carbon dioxide production. The enrichment of hydrolytic and acidogenic Porphyromonadaceae, Prevotellaceae, Ruminococcaceae and unclassified Bacteroidetes in the acidogenic reactor would have contributed to the improved sludge volatile solids degradation, and ultimately the overall 2-phase system''s performance. Syntrophic acetogenic microorganisms were absent in the acidogenic reactor but present in the downstream methanogenic reactor, indicating the retention of various metabolic pathways also found in a single-stage system. The determination of key microorganisms further expands our understanding of the complex biological functions in AD process.     

垃圾填埋场甲烷厌氧氧化作用研究进展

垃圾填埋场是温室气体甲烷的重要人为排放源之一,垃圾分解产生的甲烷会发生垂向和侧向迁移,并被氧化固定在垃圾填埋场中。研究显示与硫酸盐还原作用耦合的甲烷厌氧氧化(AOM)作用在垃圾填埋场内及其渗滤液羽状体中均可发生,形成自生碳酸盐和硫化物等沉积。因此,AOM作用是垃圾填埋场甲烷减排的重要途径之一。然而只运用气体地球化学方法与技术难以确定填埋场AOM作用的特征,而填埋场内自生碳酸盐可能保存了AOM作用的信息,但其矿物学、地球化学等特征很少有报导,还有待进一步研究确定。     

厌氧氨氧化菌与其他细菌之间的协同竞争关系

随着污水脱氮行业的蓬勃发展,各种新工艺、新理论层出不穷.厌氧氨氧化(Anammox)工艺以其独特的优点脱颖而出,成为最具应用前景的新工艺.厌氧氨氧化菌作为该过程的执行者目前已发现5属17种,本文主要对5属17种的厌氧氨氧化菌进行总结,并对厌氧氨氧化菌种内关系中的群体感应系统进行详细介绍,此外还介绍了厌氧氨氧化菌与硝化菌、反硝化菌以及厌氧甲烷氧化菌之间的协同与竞争关系.最后给出常见竞争因素对厌氧氨氧化种群结构的影响,通过控制竞争因素来实现对厌氧氨氧化种群结构的调节.本文将厌氧氨氧化菌微生物生态学与厌氧氨氧化污水处理工艺相结合,为厌氧氨氧化工艺在污水生物处理中的应用提供理论依据.     

限量曝气进水时间对硝化颗粒污泥的影响特性研究

缺氧-好氧环境的交替循环对氨氧化细菌和亚硝酸盐氧化细菌具有重要影响.本研究通过逐渐增加限量曝气进水时间(从10 min至120 min)延长缺氧时段,考察柱形SBR中硝化颗粒污泥对不同缺氧-好氧环境交替循环的响应特性.整个研究过程中,硝化颗粒污泥保持着稳定的颗粒特征,粒径大于0.8 mm的颗粒污泥占总污泥量的质量分数始终在95%以上,颗粒平均沉降速率维持在125～130 m·h-1之间.尽管缺氧时段不断延长,但NH+4-N去除率和NO-2-N累积率分别稳定在(60±5)%、(85±5)%;此外,在每个周期的曝气反应时段,NH+4-N的去除速率以及NO-2-N和NO-3-N的累积速率分别保持在90mg·(L·h)-1、70 mg·(L·h)-1和15 mg·(L·h)-1左右.以上结果表明,限量进水时间的延长及其所造成的不同时间跨度的缺氧环境对硝化颗粒污泥没有较为显著的影响.     

A comparative study on the alternating mesophilic and thermophilic two-stage anaerobic digestion of food waste

An alternating mesophilic and thermophilic two stage anaerobic digestion(AD) process was conducted. The temperature of the acidogenic(A) and methanogenic(M) reactors was controlled as follows: System 1(S1) mesophilic A-mesophilic M;(S2) mesophilic A-thermophilic M; and(S3)thermophilic A-mesophilic M. Initially, the AD reactor was acclimatized and inoculated with digester sludge. Food waste was added with the soluble chemical oxygen demand(SCOD) concentrations of41.4–47.0 g/L and volatile fatty acids of 2.0–3.2 g/L. Based on the results, the highest total chemical oxygen demand removal(86.6%) was recorded in S2 while S3 exhibited the highest SCOD removal(96.6%). Comparing S1 with S2, total solids removal increased by 0.5%; S3 on the other hand decreased by 0.1 % as compared to S1. However, volatile solids(VS) removal in S1, S2, and S3was 78.5%, 81.7%, and 79.2%, respectively. S2 also exhibited the highest CH4 content, yield, and production rate of 70.7%, 0.44 L CH4/g VSadded, and 1.23 L CH4/(L·day), respectively. Bacterial community structure revealed that the richness, diversity, evenness, and dominance of S2 were high except for the archaeal community. The terminal restriction fragments dendrogram also revealed that the microbial community of the acidogenic and methanogenic reactors in S2 was distinct. Therefore,S2 was the best among the systems for the operation of two-stage AD of food waste in terms of CH4production, nutrient removal, and microbial community structure.