4.8 Article

Importance of Combined Electrochemical Process Sequence and Electrode Arrangements: A Lab-scale Trial of Real Reverse Osmosis Landfill Leachate Concentrate

期刊

WATER RESEARCH
卷 192, 期 -, 页码 -

出版社

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.watres.2021.116849

关键词

Electrochemical process; landfill leachate; reverse osmosis concentrate; electrocoagulation; electrooxidation

资金

  1. National Natural Science Foundation of China [51638005]
  2. Hong Kong Innovation and Technology Commission [ITC-CNERC14EG03]
  3. Research Grants Council, Hong Kong SAR, China [T21-604/19-R]

向作者/读者索取更多资源

This study showed that a two-step electrochemical method combining aluminum-based electrocoagulation and simultaneous electrooxidation-electrocoagulation with a titanium-based lead dioxide anode can effectively treat refractory RO leachate concentrate (ROLC) with significantly improved biodegradability at a lower cost.
Reverse osmosis (RO) is a widely applied technique for wastewater effluent reuse and landfill leachate treatment. The latter generates a refractory RO leachate concentrate (ROLC), for which cost-effective treatment is required. This study focuses on a two-step electrochemical method consisting of aluminum-based electrocoagulation (EC), and simultaneous electrooxidation-electrocoagulation with a titanium-based lead dioxide (Ti/beta-PbO2) anode and aluminum cathode (EOEC) assembly. The sequence and electrode arrangements of the combined electrochemical process were investigated to determine the organic transformation, Ti/beta-PbO2 anode viability, and energy consumption. Series-based EC-EOEC decreased the total chemical oxygen demand (COD) from 8750 mg L-1 to 380 mg L-1, a 96% removal efficiency, in 3.5 hours at 141 A m(-2). Under a low energy consumption of 28.7 kWh kg(COD)(-1), the ROLC biodegradability (BOD5 /COD) significantly increased from 0.015 to 0.530, which was ascribed to aromatic removal (e.g.,-C = C) and an increase in -COOH functional groups. Furthermore, the rapid removal of natural organic matter and increase in pH elevation from EC suppressed the dissolution of Pb from the Ti/beta-PbO2 anode during the subsequent EOEC, thereby leaving 0.061 mg L-1 in the ROLC after treatment. The treatment cost was 3.86 USD kg(COD)(-1), which was approximately 34% lower than that of previously reported electrochemical processes for ROLC treatment. These findings obtained with a real RO concentrate provide a foundation for scaling up this new electrochemical treatment approach. (C) 2021 Elsevier Ltd. All rights reserved.

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