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Sequential anode-cathode configuration improves cathodic oxygen reduction and effluent quality of microbial fuel cells

机译:阳极-阴极的顺序配置可提高微生物燃料电池的阴极氧还原率和出水质量

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The reduction of oxygen at the cathode and the diffusion of protons from the anode to the cathode are currently perceived as two major bottlenecks of microbial fuel cells (MFCs). To address these issues, we have designed an MFC configuration in which the effluent of an acetate-fed anode was used as a feed for an aerated, biocatalysed cathode. The development of a cathodic biofilm achieved a four-fold increase of the current output compared with the non-catalysed graphite cathode, while the pH variation in the cathode compartment was reduced due to the additional transfer of protons via the liquid stream. The sequential anode-cathode configuration also provided for chemical oxygen demand (COD) polishing at the cathode by heterotrophic bacteria, with overall acetate removal consistently greater than 99%. The anode achieved an organic substrate removal of up to 2.45 kg COD/m~3 of anode liquid volume per day, at Coulombic efficiencies of 65-95%. Electron balances at the cathode revealed that the main cathodic process was oxygen reduction to water with no significant Coulombic losses. The maximal power output during polarization was 110 W/m~3 cathode liquid volume. The process could be operated in a stable way during more than 9 months of continuous operation. Excessive organic loading to the cathode should be avoided as it can reduce the long-term performance through the growth of heterotrophic bacteria.
机译:目前认为,阴极处氧气的减少以及质子从阳极向阴极的扩散是微生物燃料电池(MFCs)的两个主要瓶颈。为了解决这些问题,我们设计了一种MFC配置,其中乙酸盐喂养的阳极的出水用作充气的生物催化阴极的进料。与非催化石墨阴极相比,阴极生物膜的发展使电流输出增加了四倍,而阴极隔室中的pH变化则由于质子通过液流的额外转移而减少了。连续阳极-阴极配置还提供了异养细菌在阴极进行化学需氧量(COD)抛光的作用,总乙酸盐去除率始终大于99%。阳极每天可去除高达2.45 kg COD / m〜3阳极液体量的有机底物,库仑效率为65-95%。阴极的电子平衡表明,主要的阴极过程是将氧气还原成水,而没有明显的库仑损失。极化期间的最大功率输出为110 W / m〜3阴极液体体积。在连续运行超过9个月的过程中,该过程可以稳定地运行。应避免过多的有机负载到阴极,因为它会通过异养细菌的生长降低长期性能。

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