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Efficient pretreatment of industrial estate wastewater for biodegradability enhancement using a micro-electrolysis-circulatory system

机译:使用微电解循环系统对工业废水进行高效预处理,以提高生物降解性

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A self-made micro-electrolysis-circulatory system with the mixture regime of an upfiow bed and reactor was tested for the pretreatment of industrial estate wastewater with a low ratio of biological to chemical oxygen demand (BOD5/COD) at room temperature, 1:1 vol ratio of sponge iron (SFe)/granular activated carbon (GAC), and an intermittent process in aeration and discharge. The system efficiency was evaluated in view of the effects of various processes (hydraulic retention time (HRT), fillers/wastewater ratio (S/L) and aeration). COD reduction of about 51% was obtained for industrial estate wastewater at an S/L ratio of 25%, refluence rate of 16 L/h, HRT of 24 h, and aeration of 60 L/h as the optimal conditions. The considerable change in the calculated BOD5 /COD ratio, from 0.07 to 0.49, showed favorable application of the micro-electrolysis-circulatory system for the reductive and oxidative degradation of organic pollutants to enhance wastewater biodegradability. The reusability of the SFe was also investigated after three successive runs. On the basis of the results of Fe leaching, HRT, S/L ratio, scanning electron microscopy observation, and X-ray photoelectron spectroscopic analysis, the corrosion products facilitated by the inherent porosity of SFe played a significant role due to different oxygen conditions in the surface and internal layers. One result from the removal of organic pollutants dominated by the galvanic cell reactions between SFe and GAC was observed, and the integration coagulation in the bulk solution was mainly attributed to the leaching of Fe. The innovative approach described in this study provides a promising and economical technology for pretreatment of industrial wastewater prior to a biological process.
机译:测试了一种具有上流床和反应器混合方案的自制微电解循环系统,用于在室温下以较低的生化需氧量(BOD5 / COD)预处理工业废水:海绵铁(SFe)/颗粒活性炭(GAC)的体积比为1,充气和排放的过程是间歇性的。考虑到各种过程的影响(液压停留时间(HRT),填料/废水比(S / L)和曝气),评估了系统效率。最佳条件是,工业废水的COD降低约51%,S / L比率为25%,回流速率为16 L / h,HRT为24 h,通气量为60 L / h。计算出的BOD5 / COD比值从0.07到0.49的显着变化,表明微电解循环系统有利于有机污染物的还原和氧化降解,以提高废水的生物降解性。在连续运行三个之后,还对SFe的可重用性进行了研究。根据Fe的浸出,HRT,S / L比,扫描电子显微镜观察和X射线光电子能谱分析的结果,由于SFe的内在氧条件不同,SFe固有孔隙率促进的腐蚀产物发挥了重要作用。表面和内部层。观察到一种去除以SFe和GAC之间的原电池反应为主的有机污染物的结果,本体溶液中的集成凝结主要归因于Fe的浸出。这项研究中描述的创新方法为生物工艺之前的工业废水预处理提供了一种有前途且经济的技术。

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