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A bipolar membrane combined with ferric iron reduction as an efficient cathode system in microbial fuel cells

机译:双极膜结合三价铁还原作为微生物燃料电池中的有效阴极系统

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There is a need for alternative catalysts for oxygen reduction in the cathodic compartment of a microbial fuel cell (MFC). In this study, we show that a bipolar membrane combined with ferric iron reduction on a graphite electrode is an efficient cathode system in MFCs. A flat plate MFC with graphite felt electrodes, a volume of 1.2 L and a projected surface area of 290 cm(2) was operated in continuous mode. Ferric iron was reduced to ferrous iron in the cathodic compartment according to Fe3+ + e(-) -> Fe2+ (E-0 = + 0.77 V vs NHE, normal hydrogen electrode). This reversible electron transfer reaction considerably reduced the cathode overpotential. The low catholyte pH required to keep ferric iron soluble was maintained by using a bipolar membrane instead of the commonly used cation exchange membrane. For the MFC with cathodic ferric iron reduction, the maximum power density was 0.86 W/m(2) at a current density of 4.5 A/m(2). The Coulombic efficiency and energy recovery were 80-95% and 18-29% respectively.
机译:需要用于微生物燃料电池(MFC)的阴极隔室中的氧还原的替代催化剂。在这项研究中,我们表明在石墨电极上,双极膜与三价铁还原相结合是一种有效的阴极系统。以连续模式运行带有石墨毡电极,体积为1.2 L和投影表面积为290 cm(2)的平板MFC。根据Fe3 + + e(-)-> Fe2 +(E-0 = + 0.77 V,相对于NHE,普通氢电极),在阴极室中将三价铁还原为二价铁。这种可逆的电子转移反应大大降低了阴极的超电势。通过使用双极膜而不是通常使用的阳离子交换膜,保持了三价铁保持较低的阴极电解液pH值。对于具有阴极铁还原的MFC,在电流密度为4.5 A / m(2)时,最大功率密度为0.86 W / m(2)。库仑效率和能量回收率分别为80-95%和18-29%。

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