厌氧／缺氧SBR反硝化除磷效能的研究

采用厌氧 缺氧SBR反应器对以硝酸盐作为电子受体的反硝化除磷过程进行了研究。结果表明 ,反硝化聚磷菌完全可以在厌氧 缺氧交替运行条件下得到富集。稳定运行的厌氧 缺氧SBR反应器的反硝化除磷效率 >90 % ,出水磷浓度 <1mg L。进水COD浓度对反硝化除磷的效率影响很大 ,在COD浓度 <180mg L时 ,进水COD浓度越高 ,除磷效率也就越高。较高浓度的进水COD浓度将导致有剩余的COD进入缺氧段 ,对反硝化吸磷构成不利影响。污泥龄为 16d时 ,厌氧 缺氧SBR反应器取得稳定和理想的反硝化除磷效果。污泥龄减少到 8d ,由于反硝化聚磷菌的流失导致反硝化除磷效率的下降。当污泥龄恢复到 16d时 ,经过一段时间的运行 ,反硝化聚磷菌重新得到富集 ,除磷效率恢复到 90 %以上。     

络合吸收结合生物转化去除氮氧化物技术

介绍了络合吸收结合生物转化处理NOx 技术的基本原理和目前的研究进展情况 ,并分析了该技术处理氮氧化物存在的问题和未来发展方向     

Virus retention and transport through Al-oxide coated sand columns: effects of ionic strength and composition

Knowledge of the factors that influence the fate and transport of viruses in porous media is very important for accurately determining groundwater vulnerability and for developing protective regulations. In this study, six saturated sand column experiments were performed to examine the effects of a positively charged Al-oxide, which was coated on sand particles, on the retention and transport of viruses (phiX174 and MS-2) in background solutions of different ionic strength and composition. We found that the Al-oxide coating on sand significantly removed viruses during their transport in a phosphate buffered saline (PBS) solution. Mass balance calculations showed that 34% of the input MS-2 was inactivated/irreversibly sorbed on the surface of Al-oxide coated sand whereas 100% of phiX174 was recovered. Results from this study also indicated that higher ionic strength facilitated the transport of both phiX174 and MS-2 through the Al-oxide coated sand. This was attributed to the effect of ion shielding, which at higher ionic strength decreased the electrostatic attraction between the viral particles and the sand surface and consequently decreased virus sorption. Strong effect of the ionic strength indicates that an outer-sphere complexation mechanism was responsible for the virus sorption on the Al-oxide coated sand. Ion composition of the background solutions was also found to be a significant factor in influencing virus retention and transport. Virus transport was enhanced in the presence of phosphate (HPO(4)(2-)) as compared to bicarbonate (HCO(3)(-)), and the effect of HPO(4)(2-) was more significant on MS-2 than on phiX174. The presence of bivalent cations (Ca(2+) and Mg(2+)) increased virus transport because the cations partially screened the negative charges on the viruses therefore decreased the electrostatic attraction between the positively charged sand surface and the negatively charged viruses. Mass recovery data indicated that bivalent cations gave rise to a certain degree of inactivation/irreversibly sorption of phiX174 on the surface of Al-oxide coated sand. On the contrary, the bivalent cations appeared to have protected MS-2 from inactivation/irreversibly sorption. This study provides some insights into the mechanisms responsible for virus retention and transport in porous media.     

微絮凝-直接过滤工艺在城市污水深度处理中的应用研究

微絮凝 -直接过滤工艺是一种将混凝反应、沉淀截留集中在同一滤柱内同步完成的高效水处理工艺。该工艺应用于城市污水的深度处理中 ,通过絮凝剂的加入 ,具有同步去除PO3 -4 P、SS和部分COD的功能。本文研究了该工艺对二级处理出水中PO3 -4 P、SS和COD的去除效果及其规律。研究表明 :采用聚合氯化铁 (PFC)作为絮凝剂 ,当Fe/P摩尔比为 2∶1时 ,水中PO3 -4 P的去除率达 98.8% ,浓度可降至 0 .1mg/L以下 ,同时SS、COD去除率也有明显提高。与传统的混凝、沉淀除磷工艺相比 ,该工艺具有操作简单、结构紧凑、占地面积小、污泥量少等优点 ,是一种更为经济和简单的处理单元 ,适用于现有城市污水处理厂的除磷和进一步提高水质的深度处理     

脱木素工艺处理造纸废水的实践与机理

脱木素工艺为中小制浆企业的黑液治理提供了新的方法。系统中酸化纤维污泥减小碱木素胶粒间的斥力 ,吸附废水中已析出的木质素和细小纤维 ;酸破坏了系统中胶体的水化膜 ,增大了胶体的粒径 ;混凝剂中和胶体表面电荷 ,增加颗粒间的接触机会 ,同时发挥了絮凝沉降的作用。该工艺与传统工艺相比 ,减少了酸及混凝剂的用量 ,木素沉降速度快。当试验废水pH =5、绝干纤维污泥与进水CODCr质量之比为 1.1、硫酸铝投加量为 160mg/L时 ,CODCr去除率高于 63 %。     

碳氮磷比例失调城市污水的同步脱氮除磷

为解决现行同步脱氮除磷工艺处理南方地区碳、氮、磷比例失调城市污水中,因C/N、C/P偏低,碳源不足而降低脱氮除磷效率的难题,试验以碳源偏低的广州市城市污水为研究对象,采用厌氧/好氧交替运行的SBR系统,通过对厌氧、好氧时段的合理调控,在无需额外添加碳源的条件下,有机物、氨氮、总氮和总磷的平均去除率分别可达90%、72%、41%和99%,不仅能使有机物和氮的出水指标达到国家排放标准,而且总磷出水浓度能达0.5 mg/L以下。通过进一步分析同步高效脱氮除磷的影响因素和控制条件,得出合理污泥龄的控制是实现同步脱氮除磷的关键,厌氧/好氧交替运行的方式不仅强化了磷的释放和吸收,而且降低了碳源偏低和硝酸盐对同步脱氮除磷影响的结论。     

微囊藻毒素污染控制技术的研究进展

主要对水环境中微囊藻毒素污染的产生、毒性和去除方法进行了综述,在如何高效去除MCs方面具有重要意义.     

同步硝化反硝化生物脱氮技术研究

讨论了影响同步硝化反硝化反应的各参数,并进行了单因素实验与正交实验,获得了同步硝化反硝化生物脱氮工艺运行的最佳条件:DO浓度控制在0.5～2 mg/L,COD浓度为600～800mg/L,混合液悬浮固体(MLSS)为5000 mg/L,pH值在8.0左右,反应时间为6 h.在此条件下,氨氮及COD的去除率都较高,分别达85%和95%,总氮去除率为68 5%.     

连续流分段进水生物脱氮工艺控制要点及优化

主要介绍了分段进水生物脱氮工艺的系统工作原理及工艺特性,并探讨了该工艺运行操作和设计的几个重要影响因素,如进水流量分配比、溶解氧、污泥回流比、C/N比等,并在此基础上讨论了分段进水生物脱氮工艺的优化控制对策.     

人工湿地处理系统中多环芳烃的行为

采用Oasis HLB柱固相萃取的前处理技术,以气相色谱质谱联用仪(GC/MS)的分析方法,对我国北方永定河上游黑土洼人工湿地中多环芳烃污染的特征以及分布规律进行了研究.结果表明,该湿地系统以低环数多环芳烃污染为主,其中浓度最高的是菲和蒽,未检出高环数(5环、6环)多环芳烃.通过比较进水和出水的浓度,湿地系统总体上不能有效去除进水中的多环芳烃.但是比较不同工艺单元进出水浓度,复氧、植物根系及微生物等均影响到多环芳烃的去除效果,去除率在28%～65%之间.