Post-graduate Program in Agricultural and Environmental Engineering - Institute of Technology /Engineering Department, Federal Rural University of Rio de Janeiro, Campus Seropédica, 23890-000, Seropédica, Rio de Janeiro, RJ, Brazil.
Post-graduate Program in Agricultural and Environmental Engineering - Institute of Technology /Engineering Department, Federal Rural University of Rio de Janeiro, Campus Seropédica, 23890-000, Seropédica, Rio de Janeiro, RJ, Brazil.
J Environ Manage. 2022 Aug 1;315:115166. doi: 10.1016/j.jenvman.2022.115166. Epub 2022 May 4.
In the present research, a new technology using the application of ozone (O) together with an ultrafiltration (UF) membrane was tested for the tertiary treatment of wastewater. The primary and secondary wastewater-treatment systems were a septic tank and anaerobic filter. The experiment was divided into two stages: the first including only the application of O in the reactor, and the second, inclusion of the UF membrane. During the first stage of the study, where only the ozone was applied, a time of 40 min was chosen, with removal levels for chemical oxygen demand (COD), five-day biochemical oxygen demand (BOD), total organic carbon (TOC), turbidity and ammonium (NH) of 39.5%, 45.4%, 32.4%, 44.85% and 68.4% being recorded. During stage 2, the UF membrane inside the reactor was activated after 40 min of ozonation. The values for the removal of COD, BOD, TOC, turbidity, NH and total phosphorus were 89.13%, 95.41%, 82%, 93.4%, 14.75% and 79.67%, respectively. The use of O + UF removed 100% of total coliforms and viruses from the secondary wastewater. In accordance with North American and European guidelines, the water resulting from the treatment process is fit for reuse. The operating costs can vary between 0.859 € m and 2.440 € m depending on the cost per kWh in each country. The experiments were conducted under batch-mode conditions, further evaluations about the real scale operation would require a previous pilot stage that would develop more tools for operations specifications and their costs. The results recorded here show that the performance of this new reactor design is effective in the tertiary treatment of wastewater, and should be available for use in the near future.
在本研究中,测试了一种使用臭氧 (O) 应用与超滤 (UF) 膜的新技术,用于废水的三级处理。初级和二级废水处理系统是化粪池和厌氧过滤器。实验分为两个阶段:第一阶段仅在反应器中应用臭氧,第二阶段包括 UF 膜。在研究的第一阶段,仅应用臭氧,选择 40 分钟的时间,化学需氧量 (COD)、五日生化需氧量 (BOD)、总有机碳 (TOC)、浊度和铵 (NH) 的去除率分别为 39.5%、45.4%、32.4%、44.85%和 68.4%。在第二阶段,在臭氧氧化 40 分钟后,激活反应器内的 UF 膜。COD、BOD、TOC、浊度、NH 和总磷的去除率分别为 89.13%、95.41%、82%、93.4%、14.75%和 79.67%。O+UF 的使用从二级废水中去除了 100%的总大肠菌群和病毒。根据北美和欧洲的指南,处理过程产生的水适合再利用。运行成本根据每个国家的每千瓦时成本在 0.859 欧元/m 到 2.440 欧元/m 之间变化。实验在分批模式条件下进行,关于实际规模运行的进一步评估将需要一个前期的试点阶段,该阶段将开发更多用于操作规范及其成本的工具。这里记录的结果表明,这种新型反应器设计在废水的三级处理中性能有效,并且应该在不久的将来投入使用。