固定化微生物技术在难降解有机污染物治理中的研究进展

综述了90年代以来固定化微生物技术用于难降解有机污染物治理中的最新研究进展,这些难降解有机污染物包括:酚类(苯酚、氯代酚、甲酚、硝基酚等),芳香烃类(单环芳烃、多环芳烃、杂环芳烃)及其他化合物(酰胺类、氰、农药、杀虫剂、合成洗涤剂等)。并对固定化技术的应用前景及存在的问题进行了评述。      

Effects of residual organics in municipal wastewater on hydrogenotrophic denitrifying microbial communities

Hydrogenotrophic denitrification is promising for tertiary nitrogen removal from municipal wastewater. To reveal the influence of residual organics in municipal wastewater on hydrogenotrophic denitrifiers, we adopted high-throughput 16S rRNA gene amplicon sequencing to examine microbial communities in hydrogenotrophic denitrification enrichments. Using effluent from a municipal wastewater treatment plant as water source, COD, nitrate and pH were controlled the same except for a gradient of biodegradable carbon (i.e., primary effluent (PE), secondary effluent (SE), or combined primary and secondary effluent (CE)). Inorganic synthetic water (IW) was used as a control. Hydrogenophaga, a major facultative autotroph, accounted for 17.1%, 5.3%, 32.7% and 12.9% of the sequences in PE, CE, SE and IW, respectively, implicating that Hydrogenophaga grew well with or without organics. Thauera, which contains likely obligate autotrophic denitrifiers, appeared to be the most dominant genera (23.6%) in IW and accounted for 2.5%, 4.6% and 8.9% in PE, CE and SE, respectively. Thermomonas, which is related to heterotrophic denitrification, accounted for 4.2% and 7.9% in PE and CE fed with a higher content of labile organics, respectively. In contrast, Thermomonas was not detected in IW and accounted for only 0.6% in SE. Our results suggest that Thermomonas are more competitive than Thauera in hydrogenotrophic denitrification with biodegradable organics. Moreover, facultative autotrophic denitrifiers, Hydrogenophaga, are accommodating to residual organic in effluent wastewater, thus we propose that hydrogenotrophic denitrification is amenable for tertiary nitrogen removal.     

CMF微生物菌剂修复河流污水的动力学分析

本文利用甲壳素包裹的复合微生物菌剂CMF，对河流污水进行生物治理，CX3Dcr去除率达87．75％，BOD5去除率为86％以上。建立了河水中有机物降解的动力学模型，并通过工程实验数据，推算出了污水中有机物降解的动力学参数。     

Aromatic organic contaminant removal from an aqueous environment by p(4-VP)-based materials

p(4-vinylpyridine) (p(4-VP)) hydrogels were prepared in bulk (macro, 5 × 6 mm) and in nanosizes (370 nm) dimensions. The prepared hydrogels were used to remove organic aromatic contaminates such as 4-nitrophenol (4-NP), 2-nitrophenol (2-NP), phenol (Ph) and nitrobenzene (NB) from an aqueous environment. Important parameters affecting the absorption phenomena, such as the initial concentration of the organic species and the absorbent, absorption rate, absorption capacity, pH and the temperature of the medium, were evaluated for both hydrogel sizes. The absorption capacity of bulk and microgels were found to be 4-NP > 2-NP > Ph > NB. Furthermore, p(4-VP) microgels were embedded in poly(acrylamide) (p(AAm)) bulk hydrogel as a microgel-hydrogel interpenetrating polymer network and proved to be very practical in overcoming the difficulty of using the microgels in real applications. Moreover, it was demonstrated that separately prepared magnetic ferrite particles inserted inside p(4-VP) microgels during synthesis allowed for trouble-free removal of p(4-VP)-magnetic composite microgels from the aqueous environment by an externally applied magnetic field upon completion of their task.     

混凝/微滤工艺用于青草沙水源水厂的生产废水回用研究

本文通过混凝/微滤工艺对青草沙水源水水厂的生产废水开展了回用处理研究,分析了常规污染物、微量有机物、金属离子的去除规律和消毒副产物生成趋势.结果表明,混凝预处理可以有效减缓膜污染;组合工艺对悬浮态物质如颗粒物、细菌、大肠杆菌等有较好的去除效果,去除率均达85%以上;对溶解性成分,尤其是Al和微量有机物去除效果不佳,去除率均低于20%.生产废水膜过滤后相同的消毒剂浓度时消毒副产物的生成趋势高于砂滤池和炭滤池出水.研究认为,青草沙水源水厂的生产废水净化后回用的最佳回用点是砂滤池前或活性炭生物滤池前.     

活化沸石曝气生物滤池预处理微污染源水的研究

采用上流式活化沸石滤料曝气生物滤池(AZBAF)对杭州市某微污染地表源水进行生物预处理.结果表明,活化沸石的高效吸附作用可使AZBAF通过自然挂膜实现快速启动.在水力负荷1.2m/h,气水比为(3~1):1条件下,AZBAF对TOC和CODMn的去除率分别为40%~60%和10%~27%,尤其对小分子量(MW<1kDa)有机物具有良好的降解作用.同时系统对NH3-N的去除率保持在90%以上.污染物的去除主要发生在滤池30cm以下部分,这与其中微生物的数量和活性分布规律一致.暂时停运(5~10d和35d)对生物过滤影响较小,系统重启后可在6~8h和24h内基本恢复至原有处理水平.     

小分子有机醇强化过硫酸盐氧化水中二苯甲酮-3的研究

探究了小分子有机醇对过二硫酸盐(Peroxydisulfate, PDS)氧化降解二苯甲酮-3(Benzophenone-3, BP-3)的强化作用及反应机制.研究结果表明,4种有机醇(甲醇、丙醇、乙二醇和丙三醇)均在一定浓度范围内能有效促进过硫酸盐氧化降解BP-3,BP-3的降解速率随醇类分子碳链长度和羟基数目的增加而增加,增强效果依次为丙三醇>乙二醇>丙醇>甲醇.在低添加量时(21.9~350 μmol·L^-1),有机醇的添加增加了BP-3降解速率,但随着醇量的增加呈现出先增大后减小的趋势,例如丙三醇添加量从21.9 μmol·L^-1增加到87.6 μmol·L^-1,BP-3降解动力学常数从2.91×10^-4 s^-1提高到3.58×10^-4 s^-1,增加了0.23倍;但加入过多的醇却抑制了BP-3的降解,例如丙三醇添加量从87.6 μmol·L^-1进一步增加到350 μmol·L^-1,BP-3降解速率降低29.0%(2.54×10^-4 s^-1).反应温度也能有效促进醇的强化作用,温度从40 ℃升至60 ℃,添加丙三醇87.6 μmol·L^-1,BP-3的降解速率常数从6.84×10^-6 s^-1提高至6.69×10^-4 s^-1,提高了96.8倍.小分子有机醇主要是通过与·OH反应产生醇自由基,进一步激活过硫酸盐产生SO₄^·-,显著增加了SO₄^·-的产率,从而加速过硫酸盐降解BP-3的效率.     

氧化法预处理垃圾渗滤液技术研究及应用

由于垃圾渗滤液含有多种有毒有害的难降解的有机物,影响了生物处理效果。采用Fenton氧化法、湿式催化氧化法和电解氧化法预处理,可减少渗滤液的污染负荷,提高可生化性,在实际应用中取得良好的效果。     

生物反应器填埋条件下垃圾生物质组分的初期降解规律

在经甲烷化填埋层渗滤后的渗滤液循环回灌的新鲜垃圾填埋层内,以生物质分类表征为基础,分析了新鲜垃圾填埋层内固相各生物质组分（总糖、蛋白质、脂肪、纤维素和木质素）的初期降解规律.结果表明,垃圾中原有总糖组分和蛋白质的快速水解发酵是新鲜垃圾填埋后产生高有机质浓度渗滤液的主要机制;脂肪和纤维素的降解产物不是填埋初期高有机质浓度渗滤液的主要来源;纤维素是填埋层稳定产甲烷阶段的主要碳源,其水解速率可能是甲烷化过程的限速步骤;纤维素/木质素之质量比可作为指示填埋垃圾稳定化的指标.各生物质组分的初期降解速率常数均在0.01至0.1之间,而填埋气体中甲烷体积分数在60d内达到45%.食品垃圾组分富集的生活垃圾,应用生物反应器填埋技术时,必须具备足够的降解容量以代谢填埋初期固相中总糖和蛋白质快速水解产生的酸性液相产物.     

AQUATOX: Modeling environmental fate and ecological effects in aquatic ecosystems

AQUATOX combines aquatic ecosystem, chemical fate, and ecotoxicological constructs to obtain a truly integrative fate and effects model. It is a general, mechanistic ecological risk assessment model intended to be used to evaluate past, present, and future direct and indirect effects from various stressors including nutrients, organic wastes, sediments, toxic organic chemicals, flow, and temperature in aquatic ecosystems. The model has a very flexible structure and provides multiple analytical tools useful for evaluating ecological effects, including uncertainty analysis, nominal range sensitivity analysis, comparison of perturbed and control simulations, and graphing and tabulation of predicted concentrations, rates, and photosynthetic limitations. It can represent a full aquatic food web, including multiple genera and guilds of periphyton, phytoplankton, submersed aquatic vegetation, invertebrates, and fish and associated organic toxicants. It can model up to 20 organic chemicals simultaneously. (It does not model metals.) Modeled processes for organic toxicants include chemodynamics of neutral and ionized organic chemicals, bioaccumulation as a function of sorption and bioenergetics, biotransformation to daughter products, and sublethal and lethal toxicity. It has an extensive library of default biotic, chemical, and toxicological parameters and incorporates the ICE regression equations for estimating toxicity in numerous organisms. The model has been implemented for streams, small rivers, ponds, lakes, reservoirs, and estuaries. It is an integral part of the BASINS system with linkage to the watershed models HSPF and SWAT.