A Novel Anaerobic Electrochemical Membrane Bioreactor (AnEMBR) with Conductive Hollow-fiber Membrane for Treatment of Low-Organic Strength Solutions

被引:157
作者
Katuri, Krishna P. [1 ]
Werner, Craig M. [1 ]
Jimenez-Sandoval, Rodrigo J. [1 ]
Chen, Wei [2 ]
Jeon, Sungil [2 ]
Logan, Bruce E. [3 ]
Lai, Zhiping [2 ]
Arny, Gary L. [1 ]
Saikaly, Pascal E. [1 ]
机构
[1] King Abdullah Univ Sci & Technol, Biol & Environm Sci & Engn Div, Water Desalinat & Reuse Ctr, Thuwal 239556900, Saudi Arabia
[2] King Abdullah Univ Sci & Technol, Adv Membranes & Porous Mat Res Ctr, Thuwal 239556900, Saudi Arabia
[3] Penn State Univ, Dept Civil & Environm Engn, University Pk, PA 16802 USA
关键词
WASTE-WATER TREATMENT; MICROBIAL ELECTROLYSIS CELL; METHANE PRODUCTION; FUEL-CELL; HYDROGEN; METHANOGENESIS; REACTOR; COST;
D O I
10.1021/es504392n
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A new anaerobic treatment system that combined a microbial electrolysis cell (MEC) with membrane filtration using electrically conductive, porous, nickel-based hollow-fiber membranes (Ni-HFMs) was developed to treat low organic strength solution and recover energy in the form of biogas. This new system is called an anaerobic electrochemical membrane bioreactor (AnEMBR). The Ni-HFM served the dual function as the cathode for hydrogen evolution reaction (HER) and the membrane for filtration of the effluent. The AnEMBR system was operated for 70 days with synthetic acetate solution having a chemical oxygen demand (COD) of 320 mg/L. Removal of COD was >95% at all applied voltages tested. Up to 71% of the substrate energy was recovered at an applied voltage of 0.7 V as methane rich biogas (83% CH4; < 1% H-2) due to biological conversion of the hydrogen evoked at the cathode to methane. A combination of factors (hydrogen bubble formation, low cathode potential and localized high pH at the cathode surface) contributed to reduced membrane fouling in the AnEMBR compared to the control reactor (open circuit voltage). The net energy required to operate the AnEMBR system at an applied voltage of 0.7 V was significantly less (0.27 kWh/m(3)) than that typically needed for wastewater treatment using aerobic membrane bioreactors (1-2 kWh/m(3)).
引用
收藏
页码:12833 / 12841
页数:9
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