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Removal of chemical oxygen demand (COD) and heavy metals by catalytic ozonation-microbial fuel cell and Acidithiobacillus ferrooxidans leaching in flotation wastewater (FW)

机译:通过催化臭氧 - 微生物燃料电池和酸酐浸出在浮选废水(FW)中浸出的化学需氧量(COD)和重金属去除

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摘要

A catalytic ozonation-microbial fuel cell and Acidithiobacillus ferrooxidans leaching process was used in treating flotation wastewater to remove chemical oxygen demand (COD) and heavy metals in this study. The results indicated that when adding 1 g/L of manganese/modified activated carbon catalyst and 1.5 g/min ozone flow, the COD could be degraded from 2,043.67 mg/L to 711.4 mg/L. After that, the COD could continue decreasing down to 72.56 mg/L through an air-cathode single chamber microbial fuel cell (SCMFCs), coated with 0.4 mg/cm(2) platinum catalyst, after 15 days. Meanwhile, the maximum voltages and the ultimate power density of the SCMFCs reached 378.96 mV and 7,608.35 mW/m(2), respectively. For filter residue, when 1.2 g/L Fe3+, 10% (m/v) filter residue, and 10% Acidithiobacillus ferrooxidans were added, the copper leaching rate could reach 92.69% after 7 days if the pH values were adjusted to 1.9. Furthermore, the other heavy metals were also decreased to a level lower than the pollution control standard (Chinese standard GB3838-2002). The leaching parameters in terms of pH, redox potential, and cyclic voltammetry showed that the addition of an appropriate concentration of Fe3+ to the leaching systems was beneficial to copper dissolution.
机译:用于治疗浮选废水以除去本研究中的化学需氧量(COD)和重金属的浮选废水处理浮选废水中的催化臭氧化微生物燃料电池和酸酐脱氧氧化物浸出方法。结果表明,当加入1g / L锰/改性活性炭催化剂和1.5g / min臭氧流动时,COD可以从2,043.67mg / L降至711.4 mg / L.之后,COD可以通过空气阴极单室微生物燃料电池(SCMFC)继续下降至72.56mg / L,在15天后用0.4mg / cm(2)铂催化剂涂覆。同时,SCMFC的最大电压和最终功率密度分别达到378.96mV和7,608.35 mw / m(2)。对于过滤器残余物,当加入1.2g / L Fe 3 +,10%(M / V)过滤器残基和10%酸酐时,如果将pH值调节至1.9,则铜浸出速率可在7天后达到92.69%。此外,其他重金属也降低到低于污染控制标准的水平(中国标准GB3838-2002)。在pH,氧化还原电位和循环伏安方面的浸出参数显示,向浸出系统中添加适当的Fe3 +对铜溶解有益。

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