Reactive iron sulfide (FeS)-supported ultrafiltration for removal of mercury (Hg(II)) from water
This study investigated removal of Hg(II) from water using FeS(s) with batch and continuous contact filtration systems. For the batch system, kinetic experiments showed that removal of Hg(II) by FeS(s) was rapid at lower concentration (500 μM), but at higher concentration (1000 and 1250 μM), more ti...
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Veröffentlicht in: | Water research (Oxford) 2014-04, Vol.53, p.310-321 |
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description | This study investigated removal of Hg(II) from water using FeS(s) with batch and continuous contact filtration systems. For the batch system, kinetic experiments showed that removal of Hg(II) by FeS(s) was rapid at lower concentration (500 μM), but at higher concentration (1000 and 1250 μM), more time was required to achieve greater than 99% removal. The concentration of iron released to the solution remained relatively low, typically below 3 μM. This would theoretically present less than 1% of the Hg(II) removed. Thus, a simple exchange of Hg(II) for Fe(II) in the solid (FeS(s)) does not explain the results, but if the Fe(II) released could react to form another solids, low concentrations of Fe do not preclude a mechanism in which Hg(II) reacts to form HgS and release Fe(II). A continuous contact dead-end ultrafiltration (DE/UF) system was developed to treat water containing Hg(II) by applying a FeS(s) suspension with stirred or non-stirred modes. A major reason for applying stirring to the system was to investigate the role of “shear” flow in rejection of Hg(II)-contacted FeS(s) by a UF membrane and the stability of Hg on the FeS(s). The Hg(II)-contacted FeS(s) was completely rejected by the DE/UF system and mercury was strongly retained on the FeS(s) particles. Almost no release of Hg(II) (≈0 mM) from the FeS(s) solids was observed when they were contacted with 0.1M-thiosulfate, regardless of whether the system was operated in stirred or non-stirred mode. However, rapid oxidation of FeS(s) was observed in the stirred system but not in the non-stirred system. Determining the mechanism of oxidation requires further study, but it is important because oxidation reduces the ability of the solids to remove additional Hg(II).
Schematic representation of FeS-supported dead-end ultrafiltration system for removal of Hg(II) and flowchart of experimental procedures. [Display omitted]
•Biphasic removal pattern in kinetic removal of Hg(II) by FeS.•Successful deposition of Hg(II)-contacted FeS onto UF membrane.•Higher removal ability of non-stirred DE/UF system than stirred DE/UF system.•Less oxidation of FeS deposited on the membrane occurs at non-stirred system. |
doi_str_mv | 10.1016/j.watres.2014.01.033 |
format | Article |
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Schematic representation of FeS-supported dead-end ultrafiltration system for removal of Hg(II) and flowchart of experimental procedures. [Display omitted]
•Biphasic removal pattern in kinetic removal of Hg(II) by FeS.•Successful deposition of Hg(II)-contacted FeS onto UF membrane.•Higher removal ability of non-stirred DE/UF system than stirred DE/UF system.•Less oxidation of FeS deposited on the membrane occurs at non-stirred system.</description><identifier>ISSN: 0043-1354</identifier><identifier>EISSN: 1879-2448</identifier><identifier>DOI: 10.1016/j.watres.2014.01.033</identifier><identifier>PMID: 24530550</identifier><language>eng</language><publisher>England: Elsevier Ltd</publisher><subject>Adsorption ; Desorption ; Ferrous Compounds - chemistry ; FeS ; Kinetics ; Mackinawite ; Mercury ; Mercury - chemistry ; Oxidation-Reduction ; Ultrafiltration ; Water Pollutants, Chemical - chemistry ; Water Purification - methods</subject><ispartof>Water research (Oxford), 2014-04, Vol.53, p.310-321</ispartof><rights>2014 Elsevier Ltd</rights><rights>Copyright © 2014 Elsevier Ltd. All rights reserved.</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c362t-ec39f4c963f10c94360e4be8b6aa7dfe74cb00c6c1b110d014bbfadd9a6fa5ed3</citedby><cites>FETCH-LOGICAL-c362t-ec39f4c963f10c94360e4be8b6aa7dfe74cb00c6c1b110d014bbfadd9a6fa5ed3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://www.sciencedirect.com/science/article/pii/S0043135414000712$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,776,780,3537,27901,27902,65306</link.rule.ids><backlink>$$Uhttps://www.ncbi.nlm.nih.gov/pubmed/24530550$$D View this record in MEDLINE/PubMed$$Hfree_for_read</backlink></links><search><creatorcontrib>Han, Dong Suk</creatorcontrib><creatorcontrib>Orillano, Maria</creatorcontrib><creatorcontrib>Khodary, Ahmed</creatorcontrib><creatorcontrib>Duan, Yuhang</creatorcontrib><creatorcontrib>Batchelor, Bill</creatorcontrib><creatorcontrib>Abdel-Wahab, Ahmed</creatorcontrib><title>Reactive iron sulfide (FeS)-supported ultrafiltration for removal of mercury (Hg(II)) from water</title><title>Water research (Oxford)</title><addtitle>Water Res</addtitle><description>This study investigated removal of Hg(II) from water using FeS(s) with batch and continuous contact filtration systems. For the batch system, kinetic experiments showed that removal of Hg(II) by FeS(s) was rapid at lower concentration (500 μM), but at higher concentration (1000 and 1250 μM), more time was required to achieve greater than 99% removal. The concentration of iron released to the solution remained relatively low, typically below 3 μM. This would theoretically present less than 1% of the Hg(II) removed. Thus, a simple exchange of Hg(II) for Fe(II) in the solid (FeS(s)) does not explain the results, but if the Fe(II) released could react to form another solids, low concentrations of Fe do not preclude a mechanism in which Hg(II) reacts to form HgS and release Fe(II). A continuous contact dead-end ultrafiltration (DE/UF) system was developed to treat water containing Hg(II) by applying a FeS(s) suspension with stirred or non-stirred modes. A major reason for applying stirring to the system was to investigate the role of “shear” flow in rejection of Hg(II)-contacted FeS(s) by a UF membrane and the stability of Hg on the FeS(s). The Hg(II)-contacted FeS(s) was completely rejected by the DE/UF system and mercury was strongly retained on the FeS(s) particles. Almost no release of Hg(II) (≈0 mM) from the FeS(s) solids was observed when they were contacted with 0.1M-thiosulfate, regardless of whether the system was operated in stirred or non-stirred mode. However, rapid oxidation of FeS(s) was observed in the stirred system but not in the non-stirred system. Determining the mechanism of oxidation requires further study, but it is important because oxidation reduces the ability of the solids to remove additional Hg(II).
Schematic representation of FeS-supported dead-end ultrafiltration system for removal of Hg(II) and flowchart of experimental procedures. [Display omitted]
•Biphasic removal pattern in kinetic removal of Hg(II) by FeS.•Successful deposition of Hg(II)-contacted FeS onto UF membrane.•Higher removal ability of non-stirred DE/UF system than stirred DE/UF system.•Less oxidation of FeS deposited on the membrane occurs at non-stirred system.</description><subject>Adsorption</subject><subject>Desorption</subject><subject>Ferrous Compounds - chemistry</subject><subject>FeS</subject><subject>Kinetics</subject><subject>Mackinawite</subject><subject>Mercury</subject><subject>Mercury - chemistry</subject><subject>Oxidation-Reduction</subject><subject>Ultrafiltration</subject><subject>Water Pollutants, Chemical - chemistry</subject><subject>Water Purification - methods</subject><issn>0043-1354</issn><issn>1879-2448</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2014</creationdate><recordtype>article</recordtype><sourceid>EIF</sourceid><recordid>eNp9kD1v2zAQhomgQeIm-QdBwdEepBxFSraWAkXQNAYMBEjamaHIY0FDMt2j5MD_vjKUdsxytzzvfTyM3QrIBYjqbpu_mZ4w5QUIlYPIQcozNhOrZZ0VSq0-sRmAkpmQpbpkn1PaAkBRyPqCXRaqlFCWMGOvz2hsHw7IA8UdT0Prg0M-f8CXRZaG_T5Sj44PbU_Gh1Ptw8j5SJywiwfT8uh5h2QHOvL54-_5er1YcE-x4-N9SNfs3Js24c17v2K_Hr7_vH_MNk8_1vffNpmVVdFnaGXtla0r6QXYWskKUDW4aipjls7jUtkGwFZWNEKAG19uGm-cq03lTYlOXrH5NHdP8c-AqdddSBbb1uwwDkmLElZKClWqEVUTaimmROj1nkJn6KgF6JNbvdWTW31yq0Ho0e0Y-_K-YWg6dP9D_2SOwNcJwPHPQ0DSyQbcWXSB0PbaxfDxhr8veI2W</recordid><startdate>20140415</startdate><enddate>20140415</enddate><creator>Han, Dong Suk</creator><creator>Orillano, Maria</creator><creator>Khodary, Ahmed</creator><creator>Duan, Yuhang</creator><creator>Batchelor, Bill</creator><creator>Abdel-Wahab, Ahmed</creator><general>Elsevier Ltd</general><scope>CGR</scope><scope>CUY</scope><scope>CVF</scope><scope>ECM</scope><scope>EIF</scope><scope>NPM</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7X8</scope></search><sort><creationdate>20140415</creationdate><title>Reactive iron sulfide (FeS)-supported ultrafiltration for removal of mercury (Hg(II)) from water</title><author>Han, Dong Suk ; Orillano, Maria ; Khodary, Ahmed ; Duan, Yuhang ; Batchelor, Bill ; Abdel-Wahab, Ahmed</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c362t-ec39f4c963f10c94360e4be8b6aa7dfe74cb00c6c1b110d014bbfadd9a6fa5ed3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2014</creationdate><topic>Adsorption</topic><topic>Desorption</topic><topic>Ferrous Compounds - chemistry</topic><topic>FeS</topic><topic>Kinetics</topic><topic>Mackinawite</topic><topic>Mercury</topic><topic>Mercury - chemistry</topic><topic>Oxidation-Reduction</topic><topic>Ultrafiltration</topic><topic>Water Pollutants, Chemical - chemistry</topic><topic>Water Purification - methods</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Han, Dong Suk</creatorcontrib><creatorcontrib>Orillano, Maria</creatorcontrib><creatorcontrib>Khodary, Ahmed</creatorcontrib><creatorcontrib>Duan, Yuhang</creatorcontrib><creatorcontrib>Batchelor, Bill</creatorcontrib><creatorcontrib>Abdel-Wahab, Ahmed</creatorcontrib><collection>Medline</collection><collection>MEDLINE</collection><collection>MEDLINE (Ovid)</collection><collection>MEDLINE</collection><collection>MEDLINE</collection><collection>PubMed</collection><collection>CrossRef</collection><collection>MEDLINE - Academic</collection><jtitle>Water research (Oxford)</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Han, Dong Suk</au><au>Orillano, Maria</au><au>Khodary, Ahmed</au><au>Duan, Yuhang</au><au>Batchelor, Bill</au><au>Abdel-Wahab, Ahmed</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Reactive iron sulfide (FeS)-supported ultrafiltration for removal of mercury (Hg(II)) from water</atitle><jtitle>Water research (Oxford)</jtitle><addtitle>Water Res</addtitle><date>2014-04-15</date><risdate>2014</risdate><volume>53</volume><spage>310</spage><epage>321</epage><pages>310-321</pages><issn>0043-1354</issn><eissn>1879-2448</eissn><abstract>This study investigated removal of Hg(II) from water using FeS(s) with batch and continuous contact filtration systems. For the batch system, kinetic experiments showed that removal of Hg(II) by FeS(s) was rapid at lower concentration (500 μM), but at higher concentration (1000 and 1250 μM), more time was required to achieve greater than 99% removal. The concentration of iron released to the solution remained relatively low, typically below 3 μM. This would theoretically present less than 1% of the Hg(II) removed. Thus, a simple exchange of Hg(II) for Fe(II) in the solid (FeS(s)) does not explain the results, but if the Fe(II) released could react to form another solids, low concentrations of Fe do not preclude a mechanism in which Hg(II) reacts to form HgS and release Fe(II). A continuous contact dead-end ultrafiltration (DE/UF) system was developed to treat water containing Hg(II) by applying a FeS(s) suspension with stirred or non-stirred modes. A major reason for applying stirring to the system was to investigate the role of “shear” flow in rejection of Hg(II)-contacted FeS(s) by a UF membrane and the stability of Hg on the FeS(s). The Hg(II)-contacted FeS(s) was completely rejected by the DE/UF system and mercury was strongly retained on the FeS(s) particles. Almost no release of Hg(II) (≈0 mM) from the FeS(s) solids was observed when they were contacted with 0.1M-thiosulfate, regardless of whether the system was operated in stirred or non-stirred mode. However, rapid oxidation of FeS(s) was observed in the stirred system but not in the non-stirred system. Determining the mechanism of oxidation requires further study, but it is important because oxidation reduces the ability of the solids to remove additional Hg(II).
Schematic representation of FeS-supported dead-end ultrafiltration system for removal of Hg(II) and flowchart of experimental procedures. [Display omitted]
•Biphasic removal pattern in kinetic removal of Hg(II) by FeS.•Successful deposition of Hg(II)-contacted FeS onto UF membrane.•Higher removal ability of non-stirred DE/UF system than stirred DE/UF system.•Less oxidation of FeS deposited on the membrane occurs at non-stirred system.</abstract><cop>England</cop><pub>Elsevier Ltd</pub><pmid>24530550</pmid><doi>10.1016/j.watres.2014.01.033</doi><tpages>12</tpages></addata></record> |
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subjects | Adsorption Desorption Ferrous Compounds - chemistry FeS Kinetics Mackinawite Mercury Mercury - chemistry Oxidation-Reduction Ultrafiltration Water Pollutants, Chemical - chemistry Water Purification - methods |
title | Reactive iron sulfide (FeS)-supported ultrafiltration for removal of mercury (Hg(II)) from water |
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