Treatment of reverse osmosis concentrate using microbial electrolysis desalination and chemical production cell

被引:39
作者
Luo, Haiping [1 ]
Li, Hui [1 ]
Lu, Yaobin [1 ]
Liu, Guangli [1 ]
Zhang, Renduo [1 ]
机构
[1] Sun Yat Sen Univ, Sch Environm Sci & Engn, Guangdong Prov Key Lab Environm Pollut Control &, Guangzhou 510275, Guangdong, Peoples R China
基金
中国国家自然科学基金;
关键词
Reverse osmosis concentrate; Microbial electrolysis desalination and chemical production cell; Desalination; Energy consumption; MUNICIPAL WASTE-WATER; DISSOLVED ORGANIC-MATTER; MALIC-ACID PRODUCTION; SECONDARY EFFLUENT; ELECTROCHEMICAL OXIDATION; INORGANIC SALTS; RECLAIMED WATER; RO CONCENTRATE; SYSTEM; RECLAMATION;
D O I
10.1016/j.desal.2017.01.003
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Containing high salinity and biotoxic organic compounds, reverse osmosis (RO) concentrate from municipal wastewater treatment plants has high environmental risks. The aim of this study was to investigate the feasibility of RO concentrate treatment using the microbial electrolysis desalination and chemical production cell (MEDCC). RO concentrate Was put into the desalination chamber. Both acid production and cathode chambers contained with 1 g/L NaCl. Within 18 h operation, the maximum desalination rate of 86 +/- 7% and no significant COD removal in the RO concentrate were achieved in the MEDCC, although the humic-like and fulvic acid-like organic compoundscould transfer from the desalination chamber into the acid-production chamber. The minimum and maximum pH in the acid-production and cathode chambers reached 1.08 +/- 0.06 and 12.2 +/- 0.10, respectively. The average total energy consumption was 6.51 +/- 0.17-9.81 +/- 0.23 kWh/m(3), among which 37%-61% was provided by the bioenergy from substrate utilization. The acid and alkali recovery, COD rejection in the treated RO concentrate and low electricity consumption in the MEDCC indicate that MEDCC may be a novel method for RO concentrate treatment in practical applications. (C) 2017 Elsevier B.V. All rights reserved.
引用
收藏
页码:52 / 59
页数:8
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