Purification of metal plating rinse waters with chelating ion exchangers
A wide range of chelating ion exchangers was tested for their abilities to remove Zn, Ni, Cu and Cd from solutions simulating waste effluents from the metal-plating industry. The task was to reduce metal discharges to the environment so that metal-plating shops could keep up with the modern, more st...
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Veröffentlicht in: | Hydrometallurgy 2000-05, Vol.56 (1), p.93-108 |
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creator | Koivula, Risto Lehto, Jukka Pajo, Leena Gale, Thomas Leinonen, Heikki |
description | A wide range of chelating ion exchangers was tested for their abilities to remove Zn, Ni, Cu and Cd from solutions simulating waste effluents from the metal-plating industry. The task was to reduce metal discharges to the environment so that metal-plating shops could keep up with the modern, more stringent regulations of waste effluents. The resins were tested by batch and mini-column experiments. Decontamination factors (DFs) as high as 700 and capacities up to 3.3 meq/mL were measured at the 5% breakthrough (BT) point in mini-column tests. Complexing agents, especially cyanide, considerably reduced the performance of the resins with only a few exceptions. Ammonium seemed to improve the ion-exchange performance of some chelating resins and capacities higher than the theoretical values, given by the manufacturer, were measured. Comparative experiments between chelating, strong acid and weak acid ion-exchange resins showed that the advantage of chelating exchangers over strong and weak acid exchangers is a very low metal BT level, even as low as 2 μg/L, which is very important, especially in the end-of-pipe polishing. |
doi_str_mv | 10.1016/S0304-386X(00)00077-3 |
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Comparative experiments between chelating, strong acid and weak acid ion-exchange resins showed that the advantage of chelating exchangers over strong and weak acid exchangers is a very low metal BT level, even as low as 2 μg/L, which is very important, especially in the end-of-pipe polishing.</description><subject>Applied sciences</subject><subject>Chelating</subject><subject>Exact sciences and technology</subject><subject>Hydrometallurgy</subject><subject>Ion exchange</subject><subject>Metal plating</subject><subject>Metals. Metallurgy</subject><subject>Production of metals</subject><subject>Production of non ferrous metals. 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Metallurgy</topic><topic>Production of metals</topic><topic>Production of non ferrous metals. Process materials</topic><topic>Rinse water</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Koivula, Risto</creatorcontrib><creatorcontrib>Lehto, Jukka</creatorcontrib><creatorcontrib>Pajo, Leena</creatorcontrib><creatorcontrib>Gale, Thomas</creatorcontrib><creatorcontrib>Leinonen, Heikki</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>METADEX</collection><collection>Technology Research Database</collection><collection>Materials Research Database</collection><jtitle>Hydrometallurgy</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Koivula, Risto</au><au>Lehto, Jukka</au><au>Pajo, Leena</au><au>Gale, Thomas</au><au>Leinonen, Heikki</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Purification of metal plating rinse waters with chelating ion exchangers</atitle><jtitle>Hydrometallurgy</jtitle><date>2000-05-01</date><risdate>2000</risdate><volume>56</volume><issue>1</issue><spage>93</spage><epage>108</epage><pages>93-108</pages><issn>0304-386X</issn><eissn>1879-1158</eissn><coden>HYDRDA</coden><abstract>A wide range of chelating ion exchangers was tested for their abilities to remove Zn, Ni, Cu and Cd from solutions simulating waste effluents from the metal-plating industry. The task was to reduce metal discharges to the environment so that metal-plating shops could keep up with the modern, more stringent regulations of waste effluents. The resins were tested by batch and mini-column experiments. Decontamination factors (DFs) as high as 700 and capacities up to 3.3 meq/mL were measured at the 5% breakthrough (BT) point in mini-column tests. Complexing agents, especially cyanide, considerably reduced the performance of the resins with only a few exceptions. Ammonium seemed to improve the ion-exchange performance of some chelating resins and capacities higher than the theoretical values, given by the manufacturer, were measured. Comparative experiments between chelating, strong acid and weak acid ion-exchange resins showed that the advantage of chelating exchangers over strong and weak acid exchangers is a very low metal BT level, even as low as 2 μg/L, which is very important, especially in the end-of-pipe polishing.</abstract><cop>Amsterdam</cop><pub>Elsevier B.V</pub><doi>10.1016/S0304-386X(00)00077-3</doi><tpages>16</tpages></addata></record> |
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subjects | Applied sciences Chelating Exact sciences and technology Hydrometallurgy Ion exchange Metal plating Metals. Metallurgy Production of metals Production of non ferrous metals. Process materials Rinse water |
title | Purification of metal plating rinse waters with chelating ion exchangers |
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