臭氧氧化深度处理印染废水改造工程实例

采用"前物化-水解酸化-好氧"组合工艺处理高浓度印染废水,新增臭氧氧化工艺进行深度处理,进一步提高废水处理效率。经调试运行结果表明,新增工艺使系统出水COD_(Cr)从100mg/L降至70 mg/L,SS从50 mg/L降至28 mg/L,色度从100倍降至36倍,排放水质达到《纺织染整工业水污染物排放标准》GB 4287-2012的排放标准。通过实际运行表明该系统深度处理的出水水质稳定性好,处理效率高。     

非均相催化臭氧氧化反应机制

臭氧催化氧化作为高级氧化技术是目前水处理领域研究的热点,其中非均相臭氧催化氧化技术因其氧化能力强、降低臭氧投加量特别是能显著提高有机物矿化率等优点而备受关注。非均相催化臭氧氧化领域不断研究新的催化剂,但是其反应过程及机制更加复杂。催化臭氧氧化的性能很大程度上取决于催化剂及其表面性质。污染物在催化剂表面形成络合物,或者臭氧在催化剂表面分解产生不同的含氧物种如表面氧原子、过氧化物和羟基自由基等。本文评述了非均相臭氧催化氧化反应中存在的多种机理,主要是自由基理论、氧空位理论、表面原子氧理论、表面络合物理论和臭氧直接氧化理论。催化剂表面的羟基基团是主要的催化活性中心,本文探讨了表面羟基基团催化反应机制,得出催化剂表面性质决定其表面活性位点的特性及含量,对诱导臭氧分解产生含氧活性物种起了关键作用;概述了催化剂改性后的结构形态、比表面积及其性能和作用机制;并讨论了非均相臭氧催化氧化反应催化剂未来的发展趋势,为催化臭氧氧化污水处理技术提供了理论参考。     

二氧化氯氧化降解含氨基硫脲废水研究

叶枯宁为有机硫杀菌剂 ,可用作防治水稻百叶枯病。氨基硫脲是合成叶枯宁过程中的中间体 ,在水中可溶 ,生产废水中其浓度较高 ,对水生生物有致毒作用 ,必须限制其高浓度废水排放。目前主要采用生化法处理 ,但效果不够理想。目前用于有机废水处理的氧化剂主要有Ｃｌ2 、ＣｌＯ2 、Ｏ3、氯胺等 ,其氧化能力顺序为Ｏ3>ＣｌＯ2 >Ｃｌ2 >氯胺 ,稳定性顺序为氯胺 >ＣｌＯ2 >Ｃｌ2 >Ｏ3[1 ] ,其中ＣｌＯ2 具有氧化能力强、稳定性高 ,特别是降解有机物时不发生氯代等优点 ,已被用作酚类、苯胺类、多环芳烃、印染废水等的降解处理[3～ 7] 。我们选择Ｃ…     

臭氧氧化法及其联合技术在废水处理中的应用

臭氧具有极强的氧化能力,其反应产生的物质一般对环境污染很小。综述了臭氧处理单元的几种方式、臭氧联合技术及其在处理城市污水及工业污水中的应用,并概述了臭氧氧化技术的发展现状及趋势。     

Fenton类氧化技术处理有机废水的研究进展

Fenton类氧化技术处理有机废水是新兴的高级氧化技术。综述了微波-Fenton、超声波-Fenton等组合法、类Fenton法处理有机废水的研究情况,并对Fenton类氧化技术处理有机废水进行了展望。     

超声波辐照和臭氧氧化协同降解废水中的结晶紫

采用超声波辐照、臭氧氧化以及超声波辐照-臭氧氧化降解废水中的结晶紫;考察了废水初始pH、超声波功率和频率、氧气流量、反应温度等因素对降解效率的影响.结果表明:超声波和臭氧对结晶紫的降解具有协同作用;当废水溶液初始质量浓度为200mg.L-1、pH为10.0时,控制超声波功率和频率分别为100 W和30kHz,氧气流量为0.4L.min-1,反应温度为25℃,反应时间为90 min,则总有机碳(TOC)的去除率可达89.2%,相应的一级反应速率常数为2.38×10-2min-1.     

电化学氧化和臭氧化预处理酸性化工废水的效能研究

保持一定酸度条件下对比了电化学氧化和臭氧氧化预处理酸性化工废水的效能（废水原pH 0.85）. 结果表明,在废水中添加2 g·L^-1 NaCl电化学氧化预处理效果较佳,30 mA·cm^-2条件下电解20 min后水样的CODCr（化学需氧量）去除率达43.4%,BOD₅/COD_Cr（生化需氧量与化学需氧量的比值）值从原来的0.034上升至0.14,可生化性明显提高. 单独臭氧化仅在pH 7.0才能取得一定的预处理效能. Ti(Ⅳ)/O₃/H₂O₂高级氧化体系在pH 2.85条件下亦有较好的预处理效果,16 min后水样COD_Cr去除率达22.9%,BOD₅/COD_Cr值则提高至0.072.     

臭氧氧化优尼素红B-B染料废水及脱色动力学研究

研究了在鼓泡反应器中,臭氧氧化优尼素红B-B模拟染料废水在10~70℃范围内的脱色反应动力学.发现并解释了不同温度下出现的反应速率交叉现象,利用紫外可见分光光度法定量分析染料特征颜色(浓度)变化情况.结果表明,在不同温度下,表观脱色反应动力学都符合一级动力学规律,相关系数都达到了0.95以上.40℃下,反应速率常数为0.011 83 s~(-1),臭氧氧化脱色过程符合y=exp(0.521-0.014x+5.02×10~(-6)x~2)方程.随着温度的升高,臭氧在高温下氧化染料的反应速率小于臭氧的分解速率,低温时臭氧氧化的速率高于臭氧的分解速率,导致高温下氧化速率变慢.在40~50℃时,臭氧氧化优尼素红B-B染料废水脱色率最高,利用紫外可见分光光度法对氧化后废水进行分析,结果表明脱色率达到了99.5%.     

高分子金属卟啉光催化氧化处理废水

 将高分子金属卟啉聚中位四（4,4’－联苯二磺酰基）氧基苯基钴卟啉用于多相光催化体系,在温和条件下成功地降解了有机染料吖啶橙．实验结果表明,降解反应符合一级动力学方程lnct＝2．52052－0．56546t（R＝－0．99704）,经8h的反应以后,染料溶液完全褪色．将此光催化剂用于混合染料、染料废水、化工厂废水及生活污水的处理,脱色率可达68％,COD去除率可达58％．通过对高压汞灯、碘钨灯和自然光等各种光源进行比较,发现在太阳光照射下,金属卟啉光催化氧化降解有机污染物的效率更高、速度更快、降解更完全．     

电化学催化氧化降解含酚废水的研究进展

酚类化合物具有高毒性,难降解性,国内外研究者越来越重视含酚废水的治理.电化学催化氧化技术在降解酚类化合物方面的研究较多.作者深入探讨了电化学催化氧化技术降解酚类化合物的机理和历程,概述了一些常用阳极材料的优缺点,最后指出了该技术存在的一些问题与发展前景.     

不同电催化工艺下苯酚的降解特性

比较了苯酚在电催化阳极氧化(AE)、阴阳两极协同降解(ACE)及亚铁离子存在下阴阳两极协同催化降解(FeACE)₃种工艺下的降解及产物变化.在电流0.25A下处理2h,废水中COD的去除率在AE下仅30％,在ACE下为60％,而在FeACE下高达90％.苯酚降解的中间产物主要为对苯二酚、邻苯二酚、间苯二酚、对苯醌、顺丁烯二酸、反丁烯二酸和草酸等.在FeACE工艺下,中间产物还有甲酸.最终产物为CO₂.FeACE不仅提高了COD的去除速率,而且还有助于有毒中间产物的迅速消除,并使有机物彻底氧化,因而在环境保护中更具有应用前景.采用水杨酸作捕获剂证实了3种电催化工艺降解有机物的羟基自由基作用机理,其进攻苯环的活性顺序为:对位>邻位>间位,根据产物变化提出了苯酚降解路径.     

Comparative Effect of UV,UV/H2O2 and UV/H2O2/Fe on Terbuthylazine Degradation in Natural and Ultrapure Water

Different advanced oxidation processes (AOPs) (ultraviolet radiation, hydrogen peroxide photolysis and photo-Fenton) were applied to test the degradation of terbuthylazine in three types of water: (a) ultrapure water, (b) surface water from the Gaditana area (Los Hurones reservoir, Cádiz, Spain) and (c) groundwater from the Tempul spring in Jerez de la Frontera (Cádiz, Spain). The experiments were carried out on a laboratory scale, using two different types of reactors, batch and semi-continuous. In batch reactors, the most efficient process for the experiments carried out with both ultrapure water and underground groundwater was ultraviolet radiation, whereas for surface water from the Gaditana area, the process that obtained the best results was the photolysis of hydrogen peroxide with 2.5 mg L⁻¹ of H₂O₂. In semi-continuous reactors, the most efficient process was the photolysis of hydrogen peroxide with 2.5 mg L⁻¹ of H₂O₂ for all the matrices studied. In both types of reactors, terbuthylazine degradation percentages higher than 90% were achieved; the main difference was in the reaction time, which varied from minutes in the batch reactor to seconds in the semi-continuous reactor. In all the applied AOPs, N-terbutyl-6-hydroxy-N′ethyl-1,3,5-triazine-2,4-diamine (TBA-212) was generated as a reaction intermediate.     

Al2O3催化剂结构对催化臭氧化活性的影响

以Al₂O₃为催化剂催化臭氧化处理邻苯二甲酸二甲酯. 通过XRD、比表面积、孔结构、FTIR和活性评价等方法对催化剂的物化性质及催化活性进行了研究, 考察了焙烧温度、成型粒径对催化剂活性的影响. 结果表明, Al₂O₃催化剂对臭氧化降解邻苯二甲酸二甲酯具有很高的催化活性, 反应120 min后, 总有机碳(TOC)的去除率从单独臭氧氧化的23.9%提高到55.1%; 焙烧温度对催化剂的活性具有很大的影响, 600 ℃催化剂催化活性最高; 随着焙烧温度的升高, Al₂O₃晶型经历了从γ-Al₂O₃到θ-Al₂O₃到α-Al₂O₃的转变, 催化剂的比表面积、焙烧得到的孔容逐渐变小, 晶体粒径变大, 表面•OH数量减少, 催化活性下降. Al₂O₃成型粒径的减小, 提高了催化剂的外比表面积, 减小了内部传质扩散的影响, 从而提高了催化活性.     

铁基金属-有机骨架及其复合物高级氧化降解水中新兴有机污染物

新兴有机污染物(Emerging organic contaminants,EOCs)是对人体健康及生态环境具有潜在或实质威胁的新型化学污染物.由于其被频繁使用且能在水生生态系统中持久性存在而对水生生物健康和安全造成严重威胁,故引起大众越来越多的关注.以活性污泥法为代表的传统水处理工艺通常不足以消除这些新兴有机污染物....     

Removal of Iodine-Containing X-ray Contrast Media from Environment: The Challenge of a Total Mineralization

Iodinated X-ray contrast media (ICM) as emerging micropollutants have attracted considerable attention in recent years due to their high detected concentration in water systems. It results in environmental issues partly due to the formation of toxic by-products during the disinfection process in water treatment. Consequently, various approaches have been investigated by researchers in order to achieve ICM total mineralization. This review discusses the different methods that have been used to degrade them, with special attention to the mineralization yield and to the nature of formed by-products. The problem of pollution by ICM is discussed in the first part dedicated to the presence of ICM in the environment and its consequences. In the second part, the processes for ICM treatment including biological treatment, advanced oxidation/reductive processes, and coupled processes are reviewed in detail. The main results and mechanisms involved in each approach are described, and by-products identified during the different treatments are listed. Moreover, based on their efficiency and their cost-effectiveness, the prospects and process developments of ICM treatment are discussed.     

Stability and Removal of Benzophenone-Type UV Filters from Water Matrices by Advanced Oxidation Processes

Benzophenone (BP) type UV filters are common environmental contaminants that are posing a growing health concern due to their increasing presence in water. Different studies have evidenced the presence of benzophenones (BP, BP-1, BP-2, BP-3, BP-4, BP-9, HPB) in several environmental matrices, indicating that conventional technologies of water treatment are not able to remove them. It has also been reported that these compounds could be associated with endocrine-disrupting activities, genotoxicity, and reproductive toxicity. This review focuses on the degradation kinetics and mechanisms of benzophenone-type UV filters and their degradation products (DPs) under UV and solar irradiation and in UV-based advanced oxidation processes (AOPs) such as UV/H₂O₂, UV/persulfate, and the Fenton process. The effects of various operating parameters, such as UV irradiation including initial concentrations of H₂O₂, persulfate, and Fe²⁺, on the degradation of tested benzophenones from aqueous matrices, and conditions that allow higher degradation rates to be achieved are presented. Application of nanoparticles such as TiO₂, PbO/TiO₂, and Sb₂O₃/TiO₂ for the photocatalytic degradation of benzophenone-type UV filters was included in this review.