Department of Engineering for Innovation, University of Salento, Via Monteroni, Lecce 73100, Italy.
Chemical and Biochemical Engineering Department, University of Western Ontario, London, Ontario N6A 5B9, Canada.
Water Res. 2022 Jul 15;220:118638. doi: 10.1016/j.watres.2022.118638. Epub 2022 May 23.
This study explored process synergies attainable by integrating a vacuum ultraviolet-based advanced oxidation process with biofiltration. A comparison using granular activated carbon or granular zeolite as filtration media were examined in context of advanced wastewater treatment for potable reuse. Six biofiltration columns, three with granular activated carbon and three with granular zeolite, were operated in parallel and batch-fed daily with nitrified secondary effluent. After achieving a pseudo-steady state through the filter columns, vacuum ultraviolet treatment was applied as pre-treatment or as post-treatment, at two different applied energies (i.e., VUV-E1=1 kWh/m and VUV-E10=10 kWh/m). Once granular activated carbon had transitioned to biologically activated carbon, as determined based on soluble chemical oxygen demand removal, adsorption was still observed as the main mechanism for contaminants of emerging concern and nitrate removal. Vacuum ultraviolet pre-treatment markedly improved contaminants of emerging concern removal through the integrated system, achieving 40% at VUV-E1 and 90% at VUV-E10. When applied as post-treatment to zeolite column effluents, VUV-E1 and VUV-E10 further increased contaminants of emerging concern removal by 20% and 90%, respectively. In the zeolite system, vacuum ultraviolet pre-treatment also increased soluble chemical oxygen demand removal efficiency, indicating that higher energy vacuum ultraviolet increased biodegradability. Total prokaryotes were two-fold more abundant in biologically activated carbon than in zeolite, with vacuum ultraviolet pretreatment markedly affecting microbial diversity, both in terms of richness and composition. Media type only marginally affected microbial richness in the biofilters but showed a marked impact on structural composition. No clear relationship between compositional structure and depth was observed.
本研究探讨了将真空紫外基高级氧化工艺与生物过滤相结合所能实现的过程协同作用。在进行饮用水回用的高级废水处理方面,考察了使用颗粒活性炭或沸石作为过滤介质的比较。六个生物过滤柱,三个装有颗粒活性炭,三个装有沸石,平行运行并每天批量进料硝化二级出水。在通过过滤柱达到准稳态后,将真空紫外处理作为预处理或后处理,施加两种不同的能量(即 VUV-E1=1 kWh/m 和 VUV-E10=10 kWh/m)。一旦颗粒活性炭转变为生物活性炭,即可根据可溶解性化学需氧量去除来确定,吸附仍然是去除新兴污染物和硝酸盐的主要机制。真空紫外预处理通过集成系统显著提高了新兴污染物的去除效率,在 VUV-E1 下达到 40%,在 VUV-E10 下达到 90%。当将 VUV-E1 和 VUV-E10 作为沸石柱出水的后处理时,分别又增加了 20%和 90%的新兴污染物去除。在沸石系统中,真空紫外预处理还提高了可溶解性化学需氧量去除效率,表明更高能量的真空紫外增加了生物降解性。生物活性炭中的总原核生物数量是沸石的两倍多,真空紫外预处理显著影响微生物多样性,无论是在丰度还是组成方面。介质类型仅对生物过滤器中的微生物丰富度有轻微影响,但对结构组成有明显影响。在深度方面没有观察到组成结构与深度之间的明显关系。