Integrated system of electrocoagulation, activated sludge, and electrooxidation for the treatment of oil refinery wastewater

IF 3.9 3区 工程技术 Q3 ENERGY & FUELS Chemical Engineering and Processing - Process Intensification Pub Date : 2025-02-01 Epub Date: 2024-12-15 DOI:10.1016/j.cep.2024.110135
José Treviño-Reséndez , Mónica Razo-Negrete , Luis A. Godínez , Yunny Meas , Josué D. García-Espinoza
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Abstract

This study assessed a treatment train consisting of an electrocoagulation process (with aluminum electrodes), an activated sludge system, and an electrooxidation process using a SnO2-RuO2-IrO2|Ti anode to obtain an effluent suitable for reuse as make-up water in cooling systems. The integration of the electrochemical processes and the biological system reached the required quality limits, resulting in an effluent with chemical oxygen demand and dissolved organic carbon of 36 ± 7.8 mg L−1 and 10.2 ± 0.4 mg L−1, respectively, which complies with the 60 mg L−1 limit reported by U.S. Environmental Protection Agency in 2012. In addition, the N-NH4 and total suspended solids parameters met the limits of 1 mg L−1 and 10 mg L−1, respectively, also established by this standard. Regarding dissolved salts that can promote scale formation, the treated water had a silica concentration, measured as SiO2, of 39.8 ± 4.5 mg L−1. The reduction in calcium and total hardness was only 15–20%. The evaluation of acute toxicity by the Microtox® method showed that the toxicity of the wastewater was reduced up to 2.25% and 0.23% at 5 and 15 min of exposure, respectively, after the treatment train. The impact of primary treatment by electrocoagulation on the secondary process was also observed, showing a more stable performance in the biodegradation of organic matter, nitrification, and acute toxicity. Integrating the electrocoagulation-activated sludge-electrooxidation processes, combined with an adequate softening treatment, is suggested as a potential alternative treatment train for oil refinery wastewater to produce a suitable effluent for reuse in cooling systems. This research represents a groundbreaking innovation, combining advanced physicochemical and biological processes to enhance complex pollutant removal, reduce chemical usage and environmental impact, and a more sustainable approach to meeting stringent environmental standards.

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电混凝-活性污泥-电氧化综合系统处理炼油废水
本研究评估了由电凝工艺(铝电极)、活性污泥系统和使用SnO2-RuO2-IrO2|Ti阳极的电氧化工艺组成的处理流程,以获得适合作为冷却系统补充水再利用的废水。电化学过程和生物系统的集成达到了要求的质量限值,出水化学需氧量和溶解有机碳分别为36±7.8 mg L−1和10.2±0.4 mg L−1,符合2012年美国环境保护署报告的60 mg L−1限值。此外,N-NH4和总悬浮物参数分别满足本标准规定的1 mg L−1和10 mg L−1的限值。对于促进结垢的溶解盐,处理水的二氧化硅浓度(SiO2)为39.8±4.5 mg L−1。钙和总硬度的降低仅为15-20%。通过Microtox®方法进行的急性毒性评估表明,在处理后5和15分钟,废水的毒性分别降低了2.25%和0.23%。电絮凝一级处理对二级处理的影响也被观察到,在有机物的生物降解、硝化和急性毒性方面表现出更稳定的性能。将电混凝-活性污泥-电氧化工艺与适当的软化处理相结合,建议作为炼油厂废水的潜在替代处理方案,以产生适合冷却系统的废水。这项研究代表了一项突破性的创新,结合了先进的物理化学和生物过程,以增强复杂的污染物去除,减少化学品使用和环境影响,并以更可持续的方式满足严格的环境标准。
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来源期刊
CiteScore
7.80
自引率
9.30%
发文量
408
审稿时长
49 days
期刊介绍: Chemical Engineering and Processing: Process Intensification is intended for practicing researchers in industry and academia, working in the field of Process Engineering and related to the subject of Process Intensification.Articles published in the Journal demonstrate how novel discoveries, developments and theories in the field of Process Engineering and in particular Process Intensification may be used for analysis and design of innovative equipment and processing methods with substantially improved sustainability, efficiency and environmental performance.
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