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Scaling up microbial desalination cell system with a post-aerobic process for simultaneous wastewater treatment and seawater desalination
被引:85
|作者:
Zhang, Fei
[1
]
He, Zhen
[1
]
机构:
[1] Virginia Polytech Inst & State Univ, Dept Civil & Environm Engn, Blacksburg, VA 24061 USA
来源:
关键词:
Microbial desalination cells;
Microbial fuel cells;
Wastewater treatment;
Bioenergy;
Scaling up;
ION-EXCHANGE-RESIN;
ELECTRICITY-GENERATION;
FUEL-CELLS;
BIOELECTROCHEMICAL DESALINATION;
NITRATE REMOVAL;
ENERGY;
DENITRIFICATION;
PERFORMANCE;
RECOVERY;
DRIVEN;
D O I:
10.1016/j.desal.2015.01.009
中图分类号:
TQ [化学工业];
学科分类号:
0817 ;
摘要:
A key challenge in developing microbial desalination cells (MDC) is system scaling up. Herein, a large-scale MDC system (total liquid volume of 105 L) was developed and used as a research platform to investigate the issues associated with scaling up. Highly nonuniform performance was observed among the individual MDC modules. Multiple feeding points could enhance current generation through better substrate distribution. Applying an external voltage significantly increased current generation from 670 mA (no external voltage) to nearly 2000 mA (1.1 V applied), with the corresponding increase in salt removal rate from 3.7 to 9.2 kg m(-3) day(-1). Energy consumption for salt removal decreased with increasing the applied voltage, but wastewater treatment required more energy at the same time. The high COD input decreased current generation and thus salt removal because of growth of heterotrophic microorganisms on the cathode surface. Reducing catholyte recirculation intensity could greatly decrease energy consumption by 40-60%. (C) 2015 Elsevier B.V. All rights reserved.
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页码:28 / 34
页数:7
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