Fe and N co-doped carbon derived from melamine resin capsuled biomass as efficient oxygen reduction catalyst for air-cathode microbial fuel cells

被引:43
作者
Wang, Dongliang [1 ]
Hu, Jingping [1 ,2 ,3 ]
Yang, Jiakuan [1 ,2 ,3 ]
Xiao, Keke [1 ,2 ]
Liang, Sha [1 ,2 ]
Xu, Jikun [1 ]
Liu, Bingchuan [1 ,2 ]
Hou, Huijie [1 ,2 ]
机构
[1] Huazhong Univ Sci & Technol, Sch Environm Sci & Engn, Wuhan 430074, Peoples R China
[2] Hubei Prov Engn Lab Solid Waste Treatment Disposa, 1037 Luoyu Rd, Wuhan 430074, Hubei, Peoples R China
[3] HUST, State Key Lab Coal Combust, 1037 Luoyu Rd, Wuhan 430074, Hubei, Peoples R China
关键词
Fe/N doping; Oxygen reduction reaction; Microbial fuel cell; Power density; METAL-FREE CATALYST; POROUS CARBON; ACTIVATED CARBON; POWER OVERSHOOT; NITROGEN; ELECTROCATALYSTS; NANOPARTICLES; PERFORMANCE; PYROLYSIS; SITES;
D O I
10.1016/j.ijhydene.2019.11.201
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Cathode oxygen reduction reaction (ORR) performance is crucial for power generation of microbial fuel cells (MFCs). The current study provides a novel strategy to prepare Fe/N-doped carbon (Fe/N/C) catalyst for MFCs cathode through high temperature pyrolyzing of biomass capsuling melamine resin polymer. The obtained Fe/N/C can effectively enhance activity, selectivity and stability toward 4 e(-) ORR in pH neutral solution. Single chamber MFC with Fe/N/C air cathode produces maximum power density of 1166 mW m(-2), which is 140% higher than AC cathode. The improved performance of Fe/N/C can be attributed to the involvement of nitrogen and iron species. The excellent stability can be attributed to the preferential structure of the catalyst. The moderate porosity of the catalyst facilitates mass transfer of oxygen and protons and prevents water flooding of triple-phase boundary where ORR occurs. The biomass particles encapsulated in the catalyst act as skeletons, which prevents catalyst collapse and agglomeration. (C) 2019 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:3163 / 3175
页数:13
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