Reducing the burden of food processing washdown wastewaters using microbial fuel cells

被引:12
|
作者
Boghani, Hitesh [1 ]
Kim, Jung Rae [2 ]
Dinsdale, Richard M. [1 ]
Guwy, Alan J. [1 ]
Premier, Giuliano C. [1 ]
机构
[1] Univ South Wales, Fac Comp Engn & Sci, Sustainable Environm Res Ctr SERC, Pontypridd CF37 1DL, M Glam, Wales
[2] Pusan Natl Univ, Sch Chem & Biomol Engn, Busan 609735, South Korea
基金
英国工程与自然科学研究理事会; 英国生物技术与生命科学研究理事会;
关键词
Anaerobic processes; Biodegradation; Scale-up; Waste-water treatment; Microbial Fuel Cell (MFC); COD removal; WASTE-WATER TREATMENT; START-UP TIME; ELECTRICITY-GENERATION; POWER-GENERATION; BIOELECTROCHEMICAL SYSTEM; BIOELECTRICITY PRODUCTION; ENERGY GENERATION; CATHODE; PH; PERFORMANCE;
D O I
10.1016/j.bej.2016.10.017
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
A tubular Microbial Fuel Cell (MFC) reactor consisting of four modules (total reactor volume of 1l) was fed with food processing washdown water as a chemical oxygen demand (COD) removal process to decrease effluent pollution levels and discharge costs. Two different operational modes were tested: (A) Under static electrical loads with substrate circulated to and from different storage vessels and (B) employing maximum peak power point tracking (MPPT) whilst re-circulating substrate through a single storage vessel. After 7 cycles through the reactor, notionally equivalent to 28 concatenated tubular MFC modules, 84% of the soluble COD (960 mgl(-1)) was removed from the effluent in Mode A and 70% (800 mg l(-1)) in Mode B with MPPT. In the study, acetic acid was consumed first and propionic acid increased initially before depletion after 7 cycles, showing that higher carbohydrates were degraded during the effluent polishing process. (C) 2016 Elsevier B.V. All rights reserved.
引用
收藏
页码:210 / 217
页数:8
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