Concurrent hydrogen production and phosphorus recovery in dual chamber microbial electrolysis cell

被引:36
作者
Almatouq, Abdullah [1 ,2 ]
Babatunde, A. O. [3 ]
机构
[1] Cardiff Univ, Sch Engn, Energy & Environm Theme, Hydroenvironm Res Ctr, Queens Bldg, Cardiff CF24 3AA, S Glam, Wales
[2] Kuwait Inst Sci Res, POB 24885, Safat 13109, Kuwait
[3] Univ Leeds, Inst Publ Hlth & Environm Engn, Sch Civil Engn, Leeds LS2 9JT, W Yorkshire, England
关键词
Bio-electrochemical system; Phosphorus recovery; Microbial electrolysis cell; Struvite; Response surface methodology; STRUVITE PRECIPITATION; FUEL-CELL; BIOELECTROCHEMICAL SYSTEMS; ELECTRICITY PRODUCTION; AMMONIUM RECOVERY; REJECT WATER; WASTE-WATER; CRYSTALLIZATION; PERFORMANCE; MEMBRANE;
D O I
10.1016/j.biortech.2017.02.043
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
Concurrent hydrogen (H-2) production and phosphorus (P) recovery were investigated in dual chamber microbial electrolysis cells (MECs). The aim of the study was to explore and understand the influence of applied voltage and influent COD concentration on concurrent H-2 production and P recovery in MEC. P was efficiently precipitated at the cathode chamber and the precipitated crystals were verified as struvite, using X-ray diffraction and scanning electron microscopy analysis. The maximum P precipitation efficiency achieved by the MEC was 95%, and the maximum H-2 production rate was 0.28 m(3)-H-2/m(3)-d. Response surface methodology showed that applied voltage had a great influence on H-2 production and P recovery, while influent COD concentration had a significant effect on P recovery only. The overall energy recovery in the MEC was low and ranged from 25 +/- 1 to 37 +/- 1.7%. These results confirmed MECs capability for concurrent H-2 production and P recovery. (C) 2017 Elsevier Ltd. All rights reserved.
引用
收藏
页码:193 / 203
页数:11
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