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用于电芬顿反应器的极化活性炭过滤器作为同时吸附剂和三维型电极材料的研究。

Study of polarized activated carbon filters as simultaneous adsorbent and 3D-type electrode materials for electro-Fenton reactors.

作者信息

Robles Irma, Moreno-Rubio Gabriel, García-Espinoza Josué D, Martínez-Sánchez Carolina, Rodríguez A, Meas-Vong Yunny, Rodríguez-Valadez Francisco J, Godínez Luis A

机构信息

Centro de Investigación y Desarrollo Tecnológico en Electroquímica, Parque Tecnológico Querétaro Sanfandila, 76703, Pedro Escobedo, Querétaro, Mexico.

CONACYT - Centro de Investigación y Desarrollo Tecnológico en Electroquímica, Querétaro, Mexico.

出版信息

J Environ Chem Eng. 2020 Oct;8(5):104414. doi: 10.1016/j.jece.2020.104414.

DOI:10.1016/j.jece.2020.104414
PMID:33014705
原文链接:https://pmc.ncbi.nlm.nih.gov/articles/PMC7511598/
Abstract

Electro-Fenton (EF) based water treatment processes using activated carbon (AC) packed beds constitute an attractive approach for the development of competitive degradation technology of persistent pollutants in aqueous effluents. In this work, the results of a study aimed to assess the effect on the EF performance of different parameters of the reactor's operation are presented. By means of a factorial experimental design, the influence of the AC source (lignitic or vegetal), AC acid pre-treatment, particle size distribution and the amount of Fe loaded resin in the reactor were analyzed. From the resulting data it was found that the most influential parameter in the EF performance of the reactor is the AC source. Modest effects were observed for AC acid pre-treatment, which limits Fe ion adsorption on the AC substrate. The use of a wide particle distribution of AC particles was also found to improve inter-particle electrical contact, thus favoring the electrochemical processes that take place inside the reactor. An investigation on the effect of the amount of Fe in the reactor as well as its distribution dynamics, also revealed that an excess of Fe ions in the reactor decreases the EF performance of the system since Fe ions efficiently adsorb on the AC substrate, particularly in non- acid treated samples. The best operation conditions consisted on using un-meshed vegetable AC, without acid pretreatment in an EF reactor loaded with 0.25 g of Fe, which allowed to reach full color removal of bright blue FCP model dye in 70 min.

摘要

基于电芬顿(EF)的水处理工艺采用填充有活性炭(AC)的床层,是开发具有竞争力的废水中持久性污染物降解技术的一种有吸引力的方法。在这项工作中,展示了一项旨在评估反应器运行的不同参数对EF性能影响的研究结果。通过析因实验设计,分析了AC来源(褐煤或植物性)、AC酸预处理、粒径分布以及反应器中负载铁的树脂量的影响。从所得数据发现,反应器EF性能中最具影响力的参数是AC来源。观察到AC酸预处理有适度影响,它限制了铁离子在AC基质上的吸附。还发现使用宽粒径分布的AC颗粒可改善颗粒间的电接触,从而有利于反应器内发生的电化学过程。对反应器中铁含量及其分布动态的影响进行的研究还表明,反应器中过量的铁离子会降低系统的EF性能,因为铁离子会有效吸附在AC基质上,特别是在未进行酸处理的样品中。最佳运行条件是在装有0.25 g铁的EF反应器中使用未过筛的植物性AC,且不进行酸预处理,这能在70分钟内实现亮蓝色FCP模型染料的完全脱色。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/85b8/7511598/4df8e58f3013/gr6.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/85b8/7511598/242608ac1734/ga1.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/85b8/7511598/b4123514d0c8/gr1.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/85b8/7511598/a8f65558bbd1/gr2.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/85b8/7511598/99f79a64e556/gr3.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/85b8/7511598/9c9699a7ac81/gr4.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/85b8/7511598/079f87cf54f0/gr5.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/85b8/7511598/4df8e58f3013/gr6.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/85b8/7511598/242608ac1734/ga1.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/85b8/7511598/b4123514d0c8/gr1.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/85b8/7511598/a8f65558bbd1/gr2.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/85b8/7511598/99f79a64e556/gr3.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/85b8/7511598/9c9699a7ac81/gr4.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/85b8/7511598/079f87cf54f0/gr5.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/85b8/7511598/4df8e58f3013/gr6.jpg

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