混凝沉淀去除丙烯酸丁酯废水浊度物质

采用混凝沉淀法去除丙烯酸丁酯废水中的浊度物质,比较6种混凝剂的去除效率,确定聚合氯化铝为适宜混凝剂,并选用阳离子型聚丙烯酰胺作为助凝剂。研究结果表明,聚合氯化铝和阳离子型聚丙烯酰胺的优化投加量分别为150 mg/L和20 mg/L,优化pH值为4～5,水温20～40℃,快速搅拌速度200～400 r/min,搅拌时间1～3 min,慢速搅拌速度50～80 r/min,搅拌时间5～15 min。在以上条件下,可使出水浊度从3 000 NTU左右降至1 NTU左右,同时也实现了废水中胶体物质的大量去除。     

不同来源高浓度有机废水的集中处理

按照水质情况,将多种来源于不同工业生产过程中的高浓度有机废水划分为高悬浮固体乳化液废水、难生化高浓度有机废水、高悬浮固体不含油有机废水、含铬有机废水和杂质含量较少的乳化液废水5类,分别采用酸化破乳/Fen-ton氧化/混凝/絮凝、Fenton氧化/混凝/絮凝、混凝/絮凝、还原/混凝/絮凝、震动膜过滤技术作为生化预处理技术,并通过小试和中试验证了各技术的效果。实验结果表明,按照上述分类结果,采用不同预处理技术可以得到良好的效果,废水水质明显改善,满足继续生化处理的基本条件。各预处理生产装置处理效果稳定,同时生化系统已经稳定运行120天以上,COD去除率超过90%,出水经过低剂量的Fenton试剂处理后可达到《污水排入城镇下水道水质标准》(CJ343-2012)。     

MFC-MBR耦合系统运行效果

膜生物反应器(MBR)是一种高效的污水处理工艺,而微生物燃料电池(MFC)能有效降解污泥中的胞外生物有机质(EBOM)并回收电能.将MFC与MBR联用,建立了一套能够有效抑制膜污染同时回收电能的新系统——MFC-MBR耦合系统,MBR的剩余污泥经MFC处理后回流.以传统MBR为对照,对耦合系统中污水处理效果、膜污染情况和污泥混合液的性质进行研究.研究表明,耦合系统的污水处理效果没有明显恶化,COD去除率为94％,NH4+-N的去除率为92％.耦合系统能够有效减缓膜污染的发生,清洗周期延长了28％.污泥混合液的MLVSS/MLSS稳定在80％ ～ 88％,系统内几乎没有无机颗粒积累.松散结合态胞外聚合物(LB-EPS)降低了48％,使污泥混合液性质得到改善.较低的污泥比阻(2.69×1012m/kg)和标准化毛细吸水时间(1.67 s·L/g MLSS),证明耦合系统污泥混合液脱水性能提高了.     

臭氧催化氧化工艺深度处理印染废水

采用正交实验对催化剂NiO/γ-A12O3的制备条件进行优化,并探讨臭氧催化氧化法对于印染废水的深度处理效能.结果表明,最优的催化剂制备条件为:浸渍液浓度为3％、浸渍时间为4h、灼烧温度为450℃、灼烧时间为3h.臭氧催化氧化反应15 min时,COD浓度由84.22 mg/L降低至50.00 mg/L以下;氨氮浓度由10.88 mg/L降低至5.01 mg/L;色度去除率达到69％,明显高于单纯臭氧氧化的反应效率.     

炼油污水回用处理RO系统的稳定运行及维护

文章介绍了兰州石化公司炼油污水深度处理反渗透(RO)系统的工艺流程及维护。通过进出水电导率、产水回收率等变化情况,分析了RO系统的运行状况。得知:运用此系统,反渗透系统产水回收率达到65%～70%,系统脱盐率在99%以上,产水可以满足一级除盐水要求,实现了装置稳定运行的目标。     

污水处理厂AB法工艺改造方案的探讨

针对漳州市东区污水处理厂AB法工艺改造的目标,分析了AB法工艺的局限性,结合该污水处理厂AB法工程的现有设施,从技术上探讨了5种具有脱氮除磷功能的工艺改造方案的可行性,并得到了适合于该污水处理厂AB法工艺改造的方案。     

光催化氧化处理低浓度含醇废水实验

室内实验了TiO2紫外光催化氧化处理废水中的低浓度甲醇。通过对TiO2催化剂活性及添加方式、溶液pH、紫外光强与催化剂加量等参数优化,在TiO2加入浓度为300mg/L和120 W紫外灯照射条件下,对6.8L甲醇浓度为2.77%的低浓度含醇废水持续处理70min后,废水中的甲醇去除率可达98.31%。该实验为进一步处理低浓度含醇废水提供了方法依据。     

新农村建设污水处理工程实例

山海关区新民居污水治理工程采用水解酸化+接触氧化+曝气生物滤池为主的工艺进行污水治理,实际运行结果表明:系统运行稳定,处理出水COD≤48 mg.L-1,BOD5≤9 mg.L-1,SS≤10 mg.L-1,NH3-N≤4.5 mg.L-1,TP≤0.47 mg.L-1,处理出水达到《城镇污水处理厂污染物排放标准》(GB 18918-2002)一级A标准,出水用于农村绿化和农灌,经济效益和环境效益明显。     

Treatment of coking wastewater by an advanced Fenton oxidation process using iron powder and hydrogen peroxide

In this study the treatment of coking wastewater was investigated by an advanced Fenton oxidation process using iron powder and hydrogen peroxide. Particular attention was paid to the effect of initial pH, dosage of H₂O₂ and to improvement in biodegradation. The results showed that higher COD and total phenol removal rates were achieved with a decrease in initial pH and an increase in H₂O₂ dosage. At an initial pH of less than 6.5 and H₂O₂ concentration of 0.3 M, COD removal reached 44-50% and approximately 95% of total phenol removal was achieved at a reaction time of 1 h. The oxygen uptake rate of the effluent measured at a reaction time of 1 h increased by approximately 65% compared to that of the raw coking wastewater. This indicated that biodegradation of the coking wastewater was significantly improved. Several organic compounds, including bifuran, quinoline, resorcinol and benzofuranol were removed completely as determined by GC-MS analysis. The advanced Fenton oxidation process is an effective pretreatment method for the removal of organic pollutants from coking wastewater. This process increases biodegradation, and may be combined with a classical biological process to achieve effluent of high quality.     

Chlorinated solvents in a petrochemical wastewater treatment plant: an assessment of their removal using self-organising maps

The self-organising map approach was used to assess the efficiency of chlorinated solvent removal from petrochemical wastewater in a refinery wastewater treatment plant. Chlorinated solvents and inorganic anions (11 variables) were determined in 72 wastewater samples, collected from three different purification streams. The classification of variables identified technical solvents, brine from oil desalting and runoff sulphates as pollution sources in the refinery, affecting the quality of wastewater treatment plant influent. The classification of samples revealed the formation of five clusters: the first three clusters contained samples collected from the drainage water, process water and oiled rainwater treatment streams. The fourth cluster consisted mainly of samples collected after biological treatment, and the fifth one of samples collected after an unusual event. SOM analysis showed that the biological treatment step significantly reduced concentrations of chlorinated solvents in wastewater.