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耦合萃取-浮选与表面活性剂及电化学降解用于处理多环芳烃污染的危险废物。

Coupling extraction-flotation with surfactant and electrochemical degradation for the treatment of PAH contaminated hazardous wastes.

作者信息

Tran Lan-Huong, Drogui Patrick, Mercier Guy, Blais Jean-François

机构信息

Institut National de la Recherche Scientifique (INRS-Eau Terre et Environnement), Université du Québec, 490 Rue de la Couronne, Québec, QC G1K9A9, Canada.

出版信息

J Hazard Mater. 2009 Oct 30;170(2-3):1218-26. doi: 10.1016/j.jhazmat.2009.05.104. Epub 2009 May 28.

DOI:10.1016/j.jhazmat.2009.05.104
PMID:19525064
Abstract

The performance of a two-stage process combining extraction of polycyclic aromatic hydrocarbons (PAHs) with an amphoteric surfactant (CAS) followed by electro-oxidation of PAH-foam concentrate was studied for the decontamination of aluminum industry wastes (AIW) and polluted soils. The PAH suspensions extracted from AIW and soils were treated in a 2L-parallelepipedic electrolytic cell containing Ti/RuO2 anodes and stainless steel cathodes. Current densities varying from 4.6 to 18.5 mA cm(-2) have been tested with and without addition of a supporting electrolyte (6.25 to 50 kg Na2SO4 t(-1) of dry waste). The best performance for PAH degradation was obtained while the electrolytic cell was operated during 90 min at a current density of 9.2 mA cm(-2), with a total solids concentration of 2.0%, and in presence 12.5 kg Na(2)SO(4)t(-1). The application of the process on AIW (initial PAH content: 3424 mg kg(-1)) allowed extracting 42% of PAH, whereas 50% of PAH was electrochemically degraded in the resulting foam suspensions. By comparison, 44% to 60% of PAH was extracted from polluted soils (initial PAH content: 1758 to 4160 mg kg(-1)) and 21% to 55% of PAH was oxidized in the foam suspensions. The electrochemical treatment cost (including only electrolyte and energy consumption) recorded in the best experimental conditions varied from 99 to 188 USD $ t(-1) of soils or AIW treated.

摘要

研究了一种两阶段工艺的性能,该工艺将用两性表面活性剂(CAS)萃取多环芳烃(PAHs),然后对PAH泡沫浓缩物进行电氧化,用于铝工业废料(AIW)和污染土壤的去污。从AIW和土壤中萃取的PAH悬浮液在一个含有Ti/RuO2阳极和不锈钢阴极的2L平行六面体电解槽中进行处理。测试了在添加和不添加支持电解质(每处理1吨干废料添加6.25至50千克Na2SO4)的情况下,电流密度在4.6至18.5 mA cm(-2)之间变化时的情况。当电解槽在电流密度为9.2 mA cm(-2)下运行90分钟、总固体浓度为2.0%且存在12.5千克Na(2)SO(4)t(-1)时,获得了PAH降解的最佳性能。该工艺应用于AIW(初始PAH含量:3424 mg kg(-1))时,可以萃取出42%的PAH,而在所得的泡沫悬浮液中50%的PAH被电化学降解。相比之下,从污染土壤(初始PAH含量:1758至4160 mg kg(-1))中萃取出44%至60%的PAH,并且在泡沫悬浮液中有21%至55%的PAH被氧化。在最佳实验条件下记录的电化学处理成本(仅包括电解质和能源消耗)为每处理1吨土壤或AIW从99美元到188美元不等。

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