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Photo-Fenton and sequencing batch reactor coupled to photo-Fenton processes for textile wastewater reclamation: feasibility of reuse in dyeing processes

机译:photo-Fenton和序批式反应器与光 - Fenton工艺相结合,用于纺织废水回收:在染色工艺中重复使用的可行性

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摘要

Both photo-Fenton oxidation and the combination of aerobic sequencing batch reactor (SBR) + photo-Fenton processes were investigated in a bench-scale study to degrade and reuse a real textile wastewater with Total Organic Carbon (TOC) = 390 mg L-1, Chemical Oxygen Demand (COD) = 1560 mg L-1 O-2 and Escherichia coli = 80000 CFU mL(-1) in further dyeing processes. The independent variables considered for the evaluation of the oxidative process were temperature, H2O2 and Fe (II) concentrations. Required treated water qualities were determined by both RD 1620/2007 (Spanish Normative for wastewater reclamation and reuse) and specific water qualities for internal reuse. The best results were obtained when applying photo-Fenton process as a polishing step, where previous aerobic SBR under 1 day hydraulic retention time (HRT), gave 75% TOC reduction after 25 cycles. The further photo-Fenton process coupled under: ([Fe (II)] = 66.5 mg L-1; [H2O2] = 1518 mg L-1; T = 25 degrees C and pH = 2.7) conditions, achieved final COD and TOC reductions of 97 and 95% respectively. E. coil was fully removed according to specific normative. Finally, in order to accomplish specific water qualities for 100% internal reuse, resultant water was further conditioned by reverse osmosis and reused in bench-scale simulated dyeing processes, providing similar dyeing results in terms of K/S than those obtained by using fresh water.
机译:在台式研究中研究了光芬顿氧化和需氧顺序分批反应器(SBR)+光芬顿过程的组合,以降解和再利用总有机碳(TOC)= 390 mg L-1的真实纺织废水,在进一步的染色过程中,化学需氧量(COD)= 1560 mg L-1 O-2和大肠杆菌= 80000 CFU mL(-1)。用于评估氧化过程的独立变量是温度,H2O2和Fe(II)浓度。要求的处理后水质由RD 1620/2007(针对废水回收和再利用的西班牙规范)和内部再利用的特定水质确定。当应用光芬顿法作为抛光步骤时,可获得最佳结果,其中先前的好氧SBR在1天的水力停留时间(HRT)下经过25个循环后,TOC降低了75%。在([Fe(II)] = 66.5 mg L-1; [H2O2] = 1518 mg L-1; T = 25摄氏度和pH = 2.7)条件下偶联的进一步光芬顿工艺获得了最终的COD和TOC分别减少97%和95%。根据特定规范,将大肠杆菌完全除去。最后,为了实现100%内部回用的特定水质,通过反渗透对所得水进行进一步处理,并在工作台规模的模拟染色工艺中回用,在K / S方面提供的染色结果与使用淡水获得的染色结果相似。

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