Guangzhou Key Laboratory Environmental Catalysis and Pollution Control, Guangdong Key Laboratory of Environmental Catalysis and Health Risk Control, School of Environmental Science and Engineering, Institute of Environmental Health and Pollution Control, Guangdong University of Technology, Guangzhou 510006, China.
Guangdong Province Solid Waste Recycling and Heavy Metal Pollution Control Engineering Technology Research Center, Guangdong Polytechnic of Environmental Protection Engineering, Foshan 528216, China.
Sci Total Environ. 2020 Aug 25;732:139223. doi: 10.1016/j.scitotenv.2020.139223. Epub 2020 May 8.
Following the conventional physicochemical treatment of electroless nickel (Ni) plating wastewater (ENPW) in electroplating wastewater treatment plants, highly stable and recalcitrant coordination complexes of Ni (CCN) still remain. This results in various technical problems, leading to the treatment difficulty, poor wastewater biochemistry, and failure to meet effluent standards. Therefore, an efficient decomplexation system involving heterogeneous catalytic ozonation assisted with heavy metal chelation (O/SAO3II-MDCR) was proposed in this study for the advanced treatment of CCN. The catalyst SAO3II was characterized by various methods, which revealed the mechanism of catalytic ozonation. Hydroxyl radicals (OH) and other reactive oxygen species (ROS) groups were detected, proving that catalytic ozonation was a complicated reaction process and also a foundation process of the entire system. These ROS are vital for decomplexation via heterogeneous catalytic ozonation of the system. During the catalytic decomplexation process via ozonation, CCN first underwent gradual decomposition from a highly stable macromolecular state to a volatile micromolecular state (or even completely mineralized state). Then Ni was chelated to form an insoluble and stable chelate via competitive coordination. The optimum conditions for the O/SAO3II-MDCR system were determined by single factor static experiments. After treatment with the O/SAO3II-MDCR system, the effluent concentration of total Ni was found to be <0.1 mg L, exhibiting a removal rate of up to 95.6% and achieving effective removal of total Ni from ENPW and stably meeting the discharge standard. O/SAO3II-MDCR system can easily and hopefully be extended to practical engineering applications.
在电镀废水处理厂对化学镀镍(Ni)废水(ENPW)进行常规物理化学处理后,仍然存在高度稳定和难处理的 Ni 配合物(CCN)。这导致了各种技术问题,例如处理困难、废水生化性差以及无法达到排放标准。因此,本研究提出了一种高效的脱络合系统,涉及非均相催化臭氧化辅助重金属螯合(O/SAO3II-MDCR),用于 CCN 的深度处理。催化剂 SAO3II 采用多种方法进行了表征,揭示了催化臭氧化的机理。检测到羟基自由基(OH)和其他活性氧(ROS)基团,证明催化臭氧化是一个复杂的反应过程,也是整个系统的基础过程。这些 ROS 对于通过系统的非均相催化臭氧化进行脱络合至关重要。在通过臭氧化进行催化脱络合过程中,CCN 首先从高度稳定的高分子状态逐渐分解为易挥发的小分子状态(甚至完全矿化状态)。然后,Ni 通过竞争配位螯合形成不溶性和稳定的螯合物。通过单因素静态实验确定了 O/SAO3II-MDCR 系统的最佳条件。用 O/SAO3II-MDCR 系统处理后,出水中总 Ni 的浓度<0.1mg/L,去除率高达 95.6%,有效地从 ENPW 中去除了总 Ni,稳定地达到了排放标准。O/SAO3II-MDCR 系统可以轻松并有望扩展到实际工程应用中。