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在低离子强度的微生物燃料电池中,阴离子交换膜的界面电阻。

Interface resistances of anion exchange membranes in microbial fuel cells with low ionic strength.

机构信息

School of Environmental Science and Engineering, Gwangju Institute of Science and Technology (GIST), Buk-gu, Gwangju, Republic of Korea.

出版信息

Biosens Bioelectron. 2011 Mar 15;26(7):3266-71. doi: 10.1016/j.bios.2010.12.039. Epub 2010 Dec 31.

DOI:10.1016/j.bios.2010.12.039
PMID:21255993
Abstract

The interface resistances between an anion exchange membrane (AEM) and the solution electrolyte were measured for low buffer (or ionic strength) of electrolytes typical of microbial fuel cells (MFCs). Three AEMs (AFN, AM-1, and ACS) having different properties were tested in a flat-plate MFC to which 5-mM acetate was fed to the anode and an air-saturated phosphate buffer (PB) solution was fed to the cathode. Current density achieved in the MFCs was correlated inversely with independently measured membrane-only resistances. However, the total interfacial resistances measured by current-voltage plots were approximately two orders higher than those of the membrane-only resistances, although membranes had the same order as with the membrane-only resistance. EIS spectra showed that the resistances from electric-double layer and diffusion boundary layer were the main resistances not the membrane's resistance. The electric-double layer and diffusion boundary layer resistances of the AEMs were much larger in the 10 mM PB electrolyte, compared to 100 mM PB. EIS study also showed that the resistance of diffusion boundary layer decreased due to mechanical stirring. Therefore, the interface resistance that originates from the interaction between the membrane and the catholyte solution should be considered when designing and operating MFC processes with an AEM. The AEMs allowed transport of uncharged O(2) and acetate, but the current losses for both were low during normal MFC operation.

摘要

测量了在微生物燃料电池 (MFC) 典型的低缓冲液 (或离子强度) 条件下,阴离子交换膜 (AEM) 与溶液电解质之间的界面电阻。在平板 MFC 中测试了具有不同特性的三种 AEM(AFN、AM-1 和 ACS),向阳极中添加 5 mM 乙酸盐,并向阴极中添加空气饱和的磷酸盐缓冲液 (PB) 溶液。MFC 中实现的电流密度与通过独立测量获得的仅膜电阻呈反比。然而,通过电流-电压图测量的总界面电阻比仅膜电阻高约两个数量级,尽管膜的数量级与仅膜电阻相同。EIS 谱表明,双电层和扩散边界层的电阻是主要电阻,而不是膜的电阻。与 100 mM PB 相比,AEM 在 10 mM PB 电解质中的双电层和扩散边界层电阻要大得多。EIS 研究还表明,由于机械搅拌,扩散边界层的电阻减小。因此,在设计和操作使用 AEM 的 MFC 过程时,应考虑源自膜与阴极溶液相互作用的界面电阻。AEM 允许未带电的 O(2)和乙酸盐传输,但在正常 MFC 运行期间,两者的电流损失都很低。

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