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.     

Biodrying of municipal solid waste with high water content by combined hydrolytic-aerobic technology

The high water content of municipal solid waste(MSW)will reduce the effciency of mechanical sorting,consequently unfavorable for beneficial utilization.In this study,a combined hydrolytic-aerobic biodrying technology was introduced to remove water from MSW.The total water removals were proved to depend on the ventilation frequency and the temporal span in the hydrolytic stage. The ventilation frequency of 6 times/d was preferable in the hydrolytic stage.The hydrolytic span should not be prolonged more than ...     

西安市污水厂污泥脱水试验

文章简要介绍了城市污水厂污泥的性质,并用不同的絮凝剂对城市污水污泥进行调质,结果表明阳离子型高分子絮凝剂能够取得较好的效果,并初步分析了絮凝剂的作用机理。对选定的药品进行生产性污泥脱水试验,结果使A2/O工艺的剩余污泥的平均含水率由97.4%降低至84.0%,普通活性污泥的平均含水率由93.2%降至70%。并分析了影响城市污泥脱水的因素及污泥脱水的成本分析。     

TiO_2/陶瓷光催化自洁杀菌性能研究

为了研究陶瓷的自洁、杀菌性能,文章以普通釉面陶瓷为载体,用溶胶凝胶法在其表面负载了纳米TiO2薄膜,制备了TiO2/陶瓷,并分别以甲醛模拟废水和红城湖水进行了自洁和杀菌实验。结果表明在4W紫外灯和太阳光下,对甲醛的降解率分别达到80%以上和50%以上。海口市红城湖水样在TiO2/陶瓷作用下,以4W紫外灯和太阳光为光源的灭菌率均达99%以上。表明TiO2/陶瓷有良好的自洁和灭菌性能。     

抚河南昌段底泥重金属污染特征研究

抚河南昌段是指水系从象湖将军闸流入南昌市至滕王阁排出入赣江这一段的河流。对抚河南昌段选择7个采样点采集底泥,分别采用微波消解和五步连续萃取法对抚河底泥中的重金属进行前处理,结合ICP-OES发射光谱仪测定重金属元素的含量。结果表明,抚河南昌段从上游到下游底泥重金属污染总体趋势是逐渐加重;As的平均值1079.835mg/kg,达国家土壤环境质量三级标准的35倍;个别采样点Cu的含量超过国家土壤环境质量二级标准,个别采样点Cr的含量比国家土壤环境质量三级标准的2倍还多。各采样点Cu、Mn的形态分布图很不一致,滕王阁采样点Cu的有机物结合态(S4)最高,占75.55%,Mn的铁锰氧化物结合态(S3)也较高,占50.51%;抚河桥样品Mn的可交换态(S1)最高,占74.68%;各采样点Cu的碳酸盐结合态(S2)都较低,不足20%。残渣态(S5)以将军闸30m(Cu)、司马庙立交桥(Mn)采样点较高,分别为45.40%,45.16%。抚河底泥可用于城市绿化施肥。     

苯甲酸和苯胺的微生物降解研究

用富集培养法从废水中分别分离到能以苯甲酸和苯胺为唯一碳源和能源的菌株:LS01和AG01。文章以LS01和AG01为菌株研究了其分别降解苯甲酸和苯胺生物降解的适宜条件,包括温度、底物浓度和体系pH。在最适条件下,两种菌株的降解率均能达到85%以上。     

矿井水微量油处理工艺试验研究

通过矿井水微量油处理工艺试验,研究了混凝剂和吸附剂的最佳投加量、PAC和PAM的最佳配比、吸附接触时间等技术参数与矿井水中微量油的去除率之间的关系。实验结果表明：混凝剂PAC与PAM最佳投加量的质量浓度分别是200mg／L和2mg／L;只投加吸附荆颗粒活性碳,微量油的去除率不高,其最佳投加量质量浓度为40mg／L;吸附接触时间对微量油去除率的影响不大;采取混凝、沉淀、过滤、吸附复合工艺,矿井水中微量油的去除率能达到96％,出水清澈,浊度≤2NTU。     

上流式曝气生物滤池两种填料启动挂膜的试验研究

在相同运行条件下,对瓷粒和陶粒2种不同填料曝气生物滤池（BAF）的启动运行进行了实验研究,考察了不同填料在挂膜过程中CODCr和NH4^＋-N的去除效果及出水NO2^--N和NO3^--N质量浓度的变化。结果表明,在常温下（20～25℃）2种填料的所需的启动时间差异较大,陶粒填料所需时间为17d,而瓷粒填料别需37d。启动挂膜过程中,两者对CODCr和NH4^＋-N可达到基本相同的去除率,但所需运行时间差异较大,陶粒BAF较之瓷粒BAF稳定,且硝化效果好于瓷粒BAF．     

偶氮染料生物降解机理的研究

运用紫外光谱、液相色谱与质谱研究了偶氮染料的降解过程.通过紫外光谱分析,以酸性红B为底物测定了偶氮还原酶的酶活.以甲基红为底物,分析了偶氮染料的降解机理.提出并验证了在偶氮染料还原过程中,存在一个加氢的中间体.     

黄河水作循环水补充水在发电厂的应用

根据黄河水水质情况,具体讨论黄河水作为循环水补充水在实际应用中的一些问题,结合自己的现场经验,在循环水处理上阐述自己的观点,提出一些行之有效的措施,提高循环水的浓缩倍数,以达到经济、合理节水、保护环境的目的。