Regeneration of activated carbon adsorbent by anodic and cathodic electrochemical process

被引:26
|
作者
Santos, Danilo H. S. [1 ]
Santos, Joao P. T. S. [2 ]
Duarte, Jose L. S. [1 ,2 ]
Oliveira, Leonardo M. T. M. [1 ]
Tonholo, Josealdo
Meili, Lucas [1 ]
Zanta, Carmem L. P. S. [2 ]
机构
[1] Univ Fed Alagoas, Technol Ctr, Ave Lourival Melo Mota S-N,Campus AC Simoes, BR-57072970 Maceio, AL, Brazil
[2] Univ Fed Alagoas, Chem & Biotechnol Inst, Tabuleiro Martins, Ave Lourival Melo Mota S-N,Campus AC Simoes, BR-57072970 Maceio, AL, Brazil
关键词
Adsorption; Water treatment; Adsorbent recycling; Electrochemistry; Electrodesorption; METHYLENE-BLUE ADSORPTION; AQUEOUS-SOLUTION; PBO2; ELECTRODE; GRAPHENE OXIDE; CATIONIC DYE; TEXTILE DYES; AZO-DYES; REMOVAL; OXIDATION; PHENOL;
D O I
10.1016/j.psep.2022.01.083
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The efficiency of saturated Activated Carbon (AC) electrochemical regeneration was evaluated. Reactor configurations in cathodic/anodic process, applied current effect on the properties of AC and Methylene Blue MB-AC interactions and adsorption/desorption mechanisms were studied. The efficiency was measured by adsorption capacity adsorption/regeneration cycles and changes in the adsorbent characteristic were analyzed through FTIR, BET, Optical Microscopy (OM) and SEM before and after the regeneration. The energy consumption was analyzed to assess the economic feasibility. It was found that the electrochemical treatment was efficient in returning the AC adsorption capacity, maximum efficiencies of approximately 79% and 84% were reached when the Carbon Fiber Cloth-AC electrode was subjected to anodic and cathodic currents, respectively, at a current of 0.1 A. In addition, the material demonstrated good stability through adsorption-regeneration cycles by cathodic process, with the material's adsorption capacity being almost totally recovered for 8 consecutive cycles. The removal percentage around 80% was kept after the cycles, with optimal conditions when the electrode was subjected to cathodic currents, NaCl as electrolyte at a current of 0.1 A for 2 h. The characterization techniques provided results that allow to explain the higher and prolonged efficiency of the cathodic current. Furthermore, these reactor configurations achieved an electrical energy consumption of 2.3 and 2.1 kWh kg -1 of material for cathodic and anodic, respectively. These results indicate that the electrochemical is an economical and environmental suitable technique capable of restore carbon adsorbents to be reusable for several water treatment cycles. (c) 2022 Institution of Chemical Engineers. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:1150 / 1163
页数:14
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