液体催化燃料电池中催化剂与有机燃料通过质子交换膜的交叉渗透

Kangzhi Deng, Kai Feng, Huan Li
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摘要

生物质是一种可再生能源,通过物理和化学过程加以利用。其中,液体催化燃料电池(liquid catalytic fuel cells, LCFCs)因其能够直接利用复杂的生物质废弃物并在温和条件下发电而备受关注。LCFCs通常使用Nafion质子交换膜分离阳极电解质和阴极电解质。然而,本研究揭示了LCFCs中催化剂和燃料的跨膜迁移,导致细胞性能和有机废物降解的不精确测量。典型的LCFC以磷酸钼酸(PMo)为阳极催化剂,磷酸钼多钒酸(PMoV)为阴极催化剂,葡萄糖为燃料进行组装。在环境条件下,LCFC的最大功率密度为3.57 mW/cm2,但在5天的运行中,法拉第效率显著下降,从32%降至20%。膜分析表明,Nafion 115具有0.98至4.25 nm的孔隙,允许催化剂和有机物的迁移。渗透实验表明,浓度梯度主导着物种的迁移。葡萄糖和甘露糖的渗透率分别为1.17 × 10 - 10和1.07 × 10 - 10 cm2/s,而PMo和PMoV的渗透率较低,分别为8.91 × 10 - 11和7.44 × 10 - 12 cm2/s。电场显著加速了钒的迁移,电场驱动的渗透速率为1.48 × 10−3 cm3/(s·A)。虽然模型预测表明,在5 mA的放电下,电池将在15天内失效,但实验结果表明,电池在第8天就几乎失效了。这项工作强调了通过膜或其他系统改进来解决LCFCs渗透问题的必要性。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Crossover permeation of catalysts and organic fuels through proton exchange membrane in liquid catalytic fuel cells

Crossover permeation of catalysts and organic fuels through proton exchange membrane in liquid catalytic fuel cells
Biomass, a renewable energy source, is utilized through physical and chemical processes. Among these, liquid catalytic fuel cells (LCFCs), which commonly use Nafion proton exchange membranes to separate anolyte and catholyte, attract attention for their ability to directly utilize complex biomass wastes and generate electricity under mild conditions. However, this study reveals cross-membrane migration of catalysts and fuels in LCFCs, leading to imprecise measurement of cell performance and organic waste degradation. A typical LCFC is assembled using phosphomolybdic acid (PMo) as the anode catalyst, phosphomolybdovanadic acid (PMoV) as the cathode catalyst, and glucose as fuel. Under ambient conditions, the LCFC achieves a maximum power density of 3.57 mW/cm2, but the Faradaic efficiency declines significantly over 5 days of operation, from 32 to 20%. Membrane analysis revealed that Nafion 115 possesses pores ranging from 0.98 to 4.25 nm, allowing the migration of both catalysts and organics. Permeation experiments show that concentration gradients dominate the migration of species. Glucose and mannose have permeation rates of 1.17 × 10−10 and 1.07 × 10−10 cm2/s, respectively, while PMo and PMoV exhibit lower permeation rates of 8.91 × 10⁻11 and 7.44 × 10−12 cm2/s. The electric field significantly accelerates the migration of vanadium, with an electric field-driven permeation rate of 1.48 × 10−3 cm3/(s·A). Although model predictions suggest that the cell would fail within 15 days under a 5 mA discharge, experimental results show that the cell had already nearly failed by day 8. This work highlights the need to address permeation in LCFCs through membrane or other system improvements.
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