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通过电凝聚-电浮选联合工艺去除半导体废水中的氟化物、十二烷基硫酸钠、氨和浊度。

Removal of fluoride, SDS, ammonia and turbidity from semiconductor wastewater by combined electrocoagulation-electroflotation.

作者信息

Aoudj S, Khelifa A, Drouiche N

机构信息

CRTSE-Division CCSM, N°2, Bd Dr. Frantz Fanon, P.O. Box 140, Alger Septmerveilles, 16038, Algeria; Laboratoire de génie chimique, Département de Chimie Industrielle, Université Saad Dahlab, B.P. 270, Route de Soumaa, 09000, Blida, Algeria.

Laboratoire de génie chimique, Département de Chimie Industrielle, Université Saad Dahlab, B.P. 270, Route de Soumaa, 09000, Blida, Algeria.

出版信息

Chemosphere. 2017 Aug;180:379-387. doi: 10.1016/j.chemosphere.2017.04.045. Epub 2017 Apr 14.

DOI:10.1016/j.chemosphere.2017.04.045
PMID:28415039
Abstract

Semiconductor industry effluents contain organic and inorganic pollutants, such as sodium dodecyl sulfate (SDS), fluoride and ammonia, at high levels which consists a major environmental issue. A combined EC-EF process is proposed as a post-treatment after precipitation for simultaneous clarification and removal of pollutants. In EC step, a hybrid Fe-Al was used as the soluble anode in order to avoid supplementary EC step. EC-Fe is more suitable for SDS removal; EC-Al is more suitable for fluoride removal, while EC with hybrid Al-Fe makes a good compromise. Clarification and ammonia oxidation were achieved in the EF step. Effects of anodic material, initial pH, current, anion nature, chloride concentration and initial pollutant concentration were studied. The final concentrations may reach 0.27, 6.23 and 0.22 mg L for SDS, fluoride and ammonia respectively. These concentrations are far lower than the correspondent discharge limits. Similarly, the final turbidity was found 4.35 NTU which is lower than 5NTU and the treated water does not need further filtration before discharge. Furthermore, the EC-EF process proves to be sufficiently energy-efficient with less soluble electrode consumption.

摘要

半导体行业废水含有高浓度的有机和无机污染物,如十二烷基硫酸钠(SDS)、氟化物和氨,这构成了一个重大的环境问题。提出了一种电化学-电芬顿联合工艺作为沉淀后的后处理工艺,用于同时澄清和去除污染物。在电化学步骤中,使用混合铁-铝作为可溶性阳极,以避免额外的电化学步骤。电化学铁更适合去除SDS;电化学铝更适合去除氟化物,而混合铝-铁的电化学过程则是一个很好的折衷方案。在电芬顿步骤中实现了澄清和氨氧化。研究了阳极材料、初始pH值、电流、阴离子性质、氯化物浓度和初始污染物浓度的影响。SDS、氟化物和氨的最终浓度分别可达0.27、6.23和0.22mg/L。这些浓度远低于相应的排放限值。同样,最终浊度为4.35 NTU,低于5 NTU,处理后的水在排放前无需进一步过滤。此外,电化学-电芬顿工艺被证明具有足够的能源效率,且可溶性电极消耗较少。

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