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厌氧消化橄榄磨废水的电化学矿化。

Electrochemical mineralization of anaerobically digested olive mill wastewater.

机构信息

Laboratório Nacional de Energia e Geologia, IP, 1649-038 Lisboa, Portugal.

出版信息

Water Res. 2012 Sep 1;46(13):4217-25. doi: 10.1016/j.watres.2012.05.019. Epub 2012 May 17.

Abstract

A novel approach was developed for the energetic valorisation and treatment of olive mill wastewater (OMW), combining anaerobic digestion and electrochemical oxidation. The electrochemical treatment was proposed as the final step to mineralize the remaining OMW fraction from the anaerobic reactor. The electrooxidation of anaerobically digested OMW was investigated over dimensionally stable anodes (DSAs). RuO(2) based anode was significantly more efficient than IrO(2)-type DSA, mainly for the COD removal. IrO(2) based anode promoted a selective oxidation of phenols and colour removal. For instance, after an electrolysis charge of 10.4 × 10(4) C L(-1), COD removals of 14 and 99%, phenols removals of 91 and 100% and colour removals of 85 and 100% were obtained for IrO(2) and RuO(2) DSAs-type, respectively. The electrochemical post-treatment was effectively performed without using a supporting electrolyte and in the presence of the solids that remained from the anaerobic process. The achievement of the required effluent quality for sewer systems disposal depends on the operating conditions of the anaerobic process. Consequently, special care must be taken with the chloride and nitrogen levels that may surpass the legal discharge limits. The electrochemical oxidation over RuO(2) based DSA is an appropriate second-step treatment for OMW disposal, after the recovery of its energetic potential.

摘要

开发了一种新方法,用于对橄榄厂废水(OMW)进行能量增值和处理,结合了厌氧消化和电化学氧化。电化学处理被提议作为从厌氧反应器中矿化剩余 OMW 部分的最后步骤。在尺寸稳定阳极(DSA)上研究了厌氧消化的 OMW 的电氧化。基于 RuO2 的阳极比 IrO2 型 DSA 更有效,主要是因为 COD 的去除。基于 IrO2 的阳极促进了酚类的选择性氧化和颜色去除。例如,在 10.4 × 104 C L-1 的电解电量后,IrO2 和 RuO2 DSA 型阳极分别获得了 14%和 99%的 COD 去除率、91%和 100%的酚类去除率以及 85%和 100%的颜色去除率。电化学后处理在不使用支持电解质的情况下并且在来自厌氧过程的剩余固体存在下有效地进行。达到下水道系统处理所需的废水质量取决于厌氧过程的操作条件。因此,必须特别注意可能超过法定排放限值的氯和氮水平。在回收其能量潜力之后,基于 RuO2 的 DSA 的电化学氧化是 OMW 处置的合适的第二步处理。

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