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电渗析与电凝聚联合处理含砷和铜工业废水

Combined Electrodialysis and Electrocoagulation as Treatment for Industrial Wastewater Containing Arsenic and Copper.

作者信息

Hansen Henrik K, Gutiérrez Claudia, Leiva Gonzalez Jorge, Lazo Andrea, Hansen Marcela E, Lazo Pamela, Ottosen Lisbeth M, Ortiz Rodrigo

机构信息

Departamento de Ingeniería Química y Ambiental, Universidad Técnica Federico Santa María, Valparaíso 2390123, Chile.

Departamento de Ingeniería Química, Universidad de Santiago de Chile, Santiago de Chile 9170022, Chile.

出版信息

Membranes (Basel). 2023 Feb 23;13(3):264. doi: 10.3390/membranes13030264.

DOI:10.3390/membranes13030264
PMID:36984650
原文链接:https://pmc.ncbi.nlm.nih.gov/articles/PMC10057896/
Abstract

In copper smelting processes, acidic effluents are generated that contain inorganic contaminants such as arsenic and copper. Nowadays, the treatment of wastewater is done by physicochemical methods without copper recovery. Electrodialysis is an alternative process that can recover copper. Moreover, when electrocoagulation is applied to remove arsenic from wastewater, a more stable final sludge of less volume is obtained. The present research studies the application of a combined electrodialysis and electrocoagulation process to (1) recover Cu and (2) precipitate and remove arsenic simultaneously in the same batch reactor, using synthetic wastewater that simulates wastewater from a copper smelter. Copper and arsenic could be removed and separated by the electrodialysis part, and the electrocoagulation of arsenic was verified. With electrodialysis, the arsenic and copper removals were 67% and 100%, respectively, while 82% of the arsenic arriving at the electrocoagulation part of the cell could be precipitated and removed by this process. Initial concentrations were around 815 mg L Cu and 7700 mg L As. The optimal current was found to be 1.36 A due to the shorter treatment times necessary to get removal percentages, recovery percentages and energy/removed copper mass ratios in the same ranges as the values achieved with a current of 1.02 A. In summary, the combined process is a promising tool for simultaneous copper recovery and arsenic removal.

摘要

在铜冶炼过程中,会产生含有砷和铜等无机污染物的酸性废水。如今,废水处理采用物理化学方法,且不回收铜。电渗析是一种可以回收铜的替代工艺。此外,当采用电凝聚法去除废水中的砷时,可获得体积更小、更稳定的最终污泥。本研究使用模拟铜冶炼厂废水的合成废水,研究了电渗析和电凝聚联合工艺在(1)回收铜和(2)在同一间歇反应器中同时沉淀并去除砷方面的应用。通过电渗析部分可以去除并分离铜和砷,并且验证了砷的电凝聚效果。采用电渗析时,砷和铜的去除率分别为67%和100%,而进入电解槽电凝聚部分的砷中有82%可通过该工艺沉淀并去除。初始浓度分别约为815 mg/L铜和7700 mg/L砷。由于在与1.02 A电流下达到的值相同的范围内获得去除率、回收率和能量/去除铜质量比所需的处理时间更短,因此发现最佳电流为1.36 A。总之,该联合工艺是同时回收铜和去除砷的一种有前景的工具。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/e539/10057896/e88b90bc68e2/membranes-13-00264-g009.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/e539/10057896/c53193752935/membranes-13-00264-g001.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/e539/10057896/945ca9317dbd/membranes-13-00264-g002.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/e539/10057896/80809b744c97/membranes-13-00264-g003.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/e539/10057896/15a4c06e0b4a/membranes-13-00264-g004.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/e539/10057896/d7407f85f5bc/membranes-13-00264-g005.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/e539/10057896/980a565a4a32/membranes-13-00264-g006.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/e539/10057896/62ce2d879596/membranes-13-00264-g007.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/e539/10057896/a06e70e2d4fb/membranes-13-00264-g008.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/e539/10057896/e88b90bc68e2/membranes-13-00264-g009.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/e539/10057896/c53193752935/membranes-13-00264-g001.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/e539/10057896/945ca9317dbd/membranes-13-00264-g002.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/e539/10057896/80809b744c97/membranes-13-00264-g003.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/e539/10057896/15a4c06e0b4a/membranes-13-00264-g004.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/e539/10057896/d7407f85f5bc/membranes-13-00264-g005.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/e539/10057896/980a565a4a32/membranes-13-00264-g006.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/e539/10057896/62ce2d879596/membranes-13-00264-g007.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/e539/10057896/a06e70e2d4fb/membranes-13-00264-g008.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/e539/10057896/e88b90bc68e2/membranes-13-00264-g009.jpg

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