牡蛎壳生物滤池处理含盐污水中的硝化特性

采用牡蛎壳为曝气生物滤池填料,以含NaCl的生活污水为处理对象,在SBR操作条件下,系统考察进水NaCl浓度、曝气时间及进水pH值等对硝化性能的影响。结果表明,进水NaCl浓度为10~15 g/L时,平均氨氮去除率可稳定在97%以上;较高浓度NaCl对亚硝酸化菌活性影响较弱,对硝酸化菌活性影响较强,特别是在日曝气时间少于12 h时,其出水中亚硝氮的含率大于50%;当进水pH值在6~9变化时,反应器内pH值可稳定在6.5~7.5,硝化性能良好,表明牡蛎壳填料可为硝化反应提供碱度。     

浸润线缓慢上升对滑坡剩余推力的影响规律

地下水浸润线变化对滑坡下滑力、抗滑力和剩余推力的影响甚大。基于传力系数法,建立了浸润线缓慢上升时剩余推力改变量的计算模型,探讨了滑面倾角、浸润线角度和滑面内摩擦角与倾角正切比对浸润线缓慢上升前后滑坡剩余推力改变量的影响规律;将浸润线缓慢上升时剩余推力由增大到减小的分界点称为剩余推力变化临界点,分析了剩余推力变化达到临界点时的浸润线倾角分布规律;提出了剩余推力变化的临界线,确定了浸润线缓慢上升时剩余推力的增大区域和减小区域。     

膜生物反应器生物降解与膜分离共作用特性研究

膜生物反应器实质是生物降解与膜分离相互影响,共同作用的过程,污泥浓度与通量之间存在一定的相关关系,膜分离对生和性能尤其是细菌活性有着重要的影响,而生物反应器内细菌胞外聚合物,溶解性有机物及微细胶体可能成为形成凝胶层导致通量下降的主要因素。     

壬基酚对序批式活性污泥法处理氨氮废水系统的影响

采用序批式活性污泥法(SBR)工艺,通过向SBR反应器内投加不同浓度的壬基酚(NP),探讨其对脱氮系统的影响.结果表明,当NP质量浓度为10 mg/L时,对氨氮的去除产生抑制,但并不明显,氨氮去除率仍可达约90％,在反硝化过程中,SBR反应器内会累积大量的NO2--N,对总氮的去除产生较大影响,总氮去除率只有50％,NO3--N的生成量不稳定;随着NP浓度的增加,对氨氮的去除产生抑制作用更为明显,当NP质量浓度达到80 mg/L时,氨氮去除率只有约60％,总氮去除率达到最低,只有23％.     

农药生产废水处理方法与资源化技术

综述了农药生产废水的常用处理方法和资源化技术 ,认为在处理废水的同时 ,应尽可能地回收和利用废水中有用物质 ;同时 ,要合理采用综合处理技术 ,以期达到最佳的处理效果     

河口岛屿农村地区原位与分散生活污水处理模式的环境与经济对比分析

农村污水排放所导致的环境问题日益突出,各地均大力推动污水处理模式的建立与优化.但农村污水处理模式综合效能评价体系匮乏,且多以处理工艺为主,少量考虑了管网收集系统的环境经济影响.另外,河口岛屿因其独特的自然区位,生态更加脆弱敏感,研究其污水处理问题更具有价值与意义.因此,本研究选取河口岛屿为研究对象,以崇明为例,运用生命周期评价和经济性分析理论,对比分析了分散与原位两种生活污水处理模式,包含收集和处理系统两个子系统,以及建设和运行两个阶段的环境影响与经济性.结果表明：原位和分散模式环境影响总值分别为1.75×10^-11和0.66,分散模式更具环境优势;户均成本分别为1.80万元和1.66万元,相比原位模式而言,在相同去除效果条件下,分散模式处理更有利于节约单位投资费用;处理系统为污水处理模式主要环境影响贡献子系统,其运行阶段为主要贡献阶段,且收集系统更有环境无害化和经济优势;海洋生态毒性潜值和人体毒性潜值为主要环境影响类型.     

Biodegradation of nonylphenol polyethoxylates under Fe(III)-reducing conditions

Biodegradation behavior of nonylphenol polyethoxylates (NPEOs) under Fe(III)-reducing conditions was investigated. The study demonstrated that NPEOs could be rapidly biodegraded under Fe(III)-reducing conditions. Almost 60% of the total NPEOs were removed within three days and the maximum biodegradation rate was 34.95+/-0.84 microM d(-1). NPEOs were degraded via sequential removal of ether units under Fe(III)-reducing conditions. No nonylphenol polyethoxy-carboxylates (NPECs) were formed in this process. This ether removal process was coupled to Fe(III) reduction. Nonylphenol (NP), nonylphenol monoethoxylate (NP1EO), and nonylphenol diethoxylate (NP2EO) slightly accumulated in the anaerobic biodegradation process. The accumulation of these estrogenic metabolites led to a significant increase in the estrogenic activity during the biodegradation period. The calculated estrogenic activity reached its top on day 14 when the total concentration of these estrogenic metabolites was maximal. This is the first report of the primary biodegradation behavior of NPEOs under Fe(III)-reducing conditions. These findings are of major environmental importance in terms of the environmental behavior of NPEO contaminants in natural environment.     

Mn@海藻酸微球吸附去除盐酸四环素及其类Fenton再生

以海藻酸钠为基体,制备出了Mn@海藻酸复合吸附剂.采用FE-SEM、EDS和FT-IR对产品的结构进行了表征,研究了Mn@海藻酸复合吸附剂吸附去除盐酸四环素水溶液的过程,主要考察了溶液初始浓度、p H和吸附时间对盐酸四环素吸附过程的影响,同时进行了动力学、等温模型和热力学分析,并对吸附剂的再生进行了评价.结果表明,盐酸四环素溶液初始浓度越大,平衡吸附量越大;强酸不利于Mn@海藻酸微球吸附反应的进行;随着时间的延长,吸附量呈逐渐增加的趋势.动力学模拟结果表明,吸附过程符合准二级动力学模型,等温吸附曲线符合Langmuir等温模型;热力学参数ΔG0,ΔH0,ΔS0,表明该吸附过程为自发吸热过程.通过构造Fenton-like反应体系,表面富集有盐酸四环素的Mn@海藻酸微球吸附剂可有效实现原位再生,重复使用.研究结果对含盐酸四环素废水的处理提供重要的理论依据.     

Emergency membrane contactor based absorption system for ammonia leaks in water treatment plants

Because of the suspected health risks of trihalomethanes (THMs), more and more water treatment plants have replaced traditionalchlorine disinfection process with chloramines but often without the proper absorption system installed in the case of ammonia leaksin the storage room. A pilot plant membrane absorption system was developed and installed in a water treatment plant for this purpose.Experimentally determined contact angle, surface tension, and corrosion tests indicated that the sulfuric acid was the proper choice as the absorbent for leaking ammonia using polypropylene hollow fiber membrane contactor. Effects of several operating conditionson the mass transfer coefficient, ammonia absorption, and removal efficiency were examined, including the liquid concentration,liquid velocity, and feed gas concentration. Under the operation conditions investigated, the gas absorption efficiency over 99.9%was achieved. This indicated that the designed pilot plant membrane absorption system was effective to absorb the leaking ammonia in the model storage room. The removal rate of the ammonia in the model storage room was also experimentally and theoretically foundto be primarily determined by the ammonia suction flow rate from the ammonia storage room to the membrane contactor. The ammoniaremoval rate of 99.9% was expected to be achieved within 1.3 h at the ammonia gas flow rate of 500 m3/h. The success of the pilot plantmembrane absorption system developed in this study illustrated the potential of this technology for ammonia leaks in water treatmentplant, also paved the way towards a larger scale application.