Three-Step Catalytic Detoxification Process of Wastewater Containing Chlorinated Aromatic Compounds: Experimental Results and Modeling Issues
Detoxification of water containing chlorinated aromatic compounds is performed in a single fixed bed using a periodic sequence of three steps: transient adsorption, catalytic hydrogenation, and thermal regeneration. The solid is both the adsorbent (activated carbon) and the catalyst (2.6% ruthenium...
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Veröffentlicht in: | Industrial & engineering chemistry research 1999-11, Vol.38 (11), p.4213-4219 |
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creator | Felis, Vincent Fouilloux, Pierre De Bellefon, Claude Schweich, Daniel |
description | Detoxification of water containing chlorinated aromatic compounds is performed in a single fixed bed using a periodic sequence of three steps: transient adsorption, catalytic hydrogenation, and thermal regeneration. The solid is both the adsorbent (activated carbon) and the catalyst (2.6% ruthenium loading). For chlorophenols, the end products are cyclohexanol and sodium chloride diluted in less than 2% of the amount of processed water. Adsorption is the critical step. The whole breakthrough curve is easily modeled. Conversely, the model fails to describe the early beginning which governs the purity of the effluent. The reaction step is performed under mild conditions (T < 353 K, P < 0.4 MPa) and is governed by the transient desorption of the pollutant, the catalytic reaction, and the mass-transfer processes. Thermal regeneration under hydrogen flow restores the adsorbent capacity and catalytic activity. |
doi_str_mv | 10.1021/ie990048p |
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The solid is both the adsorbent (activated carbon) and the catalyst (2.6% ruthenium loading). For chlorophenols, the end products are cyclohexanol and sodium chloride diluted in less than 2% of the amount of processed water. Adsorption is the critical step. The whole breakthrough curve is easily modeled. Conversely, the model fails to describe the early beginning which governs the purity of the effluent. The reaction step is performed under mild conditions (T < 353 K, P < 0.4 MPa) and is governed by the transient desorption of the pollutant, the catalytic reaction, and the mass-transfer processes. Thermal regeneration under hydrogen flow restores the adsorbent capacity and catalytic activity.</description><identifier>ISSN: 0888-5885</identifier><identifier>EISSN: 1520-5045</identifier><identifier>DOI: 10.1021/ie990048p</identifier><identifier>CODEN: IECRED</identifier><language>eng</language><publisher>Washington, DC: American Chemical Society</publisher><subject>ACTIVATED CARBON ; ADSORPTION ; Applied sciences ; CATALYTIC EFFECTS ; CHLORINATED AROMATIC HYDROCARBONS ; DETOXIFICATION ; ENERGY CONSERVATION, CONSUMPTION, AND UTILIZATION ; ENVIRONMENTAL SCIENCES ; Exact sciences and technology ; General purification processes ; HYDROGENATION ; MATHEMATICAL MODELS ; Pollution ; REGENERATION ; RUTHENIUM ; WASTE WATER ; Wastewaters ; Water treatment and pollution</subject><ispartof>Industrial & engineering chemistry research, 1999-11, Vol.38 (11), p.4213-4219</ispartof><rights>Copyright © 1999 American Chemical Society</rights><rights>1999 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-a421t-d84980531f61d866c77c111149ba1c17d5498f2f05a7aecc36e1a77d2a3a4a373</citedby><cites>FETCH-LOGICAL-a421t-d84980531f61d866c77c111149ba1c17d5498f2f05a7aecc36e1a77d2a3a4a373</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://pubs.acs.org/doi/pdf/10.1021/ie990048p$$EPDF$$P50$$Gacs$$H</linktopdf><linktohtml>$$Uhttps://pubs.acs.org/doi/10.1021/ie990048p$$EHTML$$P50$$Gacs$$H</linktohtml><link.rule.ids>230,314,776,780,881,2752,27053,27901,27902,56713,56763</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=1991891$$DView record in Pascal Francis$$Hfree_for_read</backlink><backlink>$$Uhttps://www.osti.gov/biblio/20003878$$D View this record in Osti.gov$$Hfree_for_read</backlink></links><search><creatorcontrib>Felis, Vincent</creatorcontrib><creatorcontrib>Fouilloux, Pierre</creatorcontrib><creatorcontrib>De Bellefon, Claude</creatorcontrib><creatorcontrib>Schweich, Daniel</creatorcontrib><creatorcontrib>Lab. de Genie des Procedes Catalytiques, Villeurbanne (FR)</creatorcontrib><title>Three-Step Catalytic Detoxification Process of Wastewater Containing Chlorinated Aromatic Compounds: Experimental Results and Modeling Issues</title><title>Industrial & engineering chemistry research</title><addtitle>Ind. Eng. Chem. Res</addtitle><description>Detoxification of water containing chlorinated aromatic compounds is performed in a single fixed bed using a periodic sequence of three steps: transient adsorption, catalytic hydrogenation, and thermal regeneration. The solid is both the adsorbent (activated carbon) and the catalyst (2.6% ruthenium loading). For chlorophenols, the end products are cyclohexanol and sodium chloride diluted in less than 2% of the amount of processed water. Adsorption is the critical step. The whole breakthrough curve is easily modeled. Conversely, the model fails to describe the early beginning which governs the purity of the effluent. The reaction step is performed under mild conditions (T < 353 K, P < 0.4 MPa) and is governed by the transient desorption of the pollutant, the catalytic reaction, and the mass-transfer processes. Thermal regeneration under hydrogen flow restores the adsorbent capacity and catalytic activity.</description><subject>ACTIVATED CARBON</subject><subject>ADSORPTION</subject><subject>Applied sciences</subject><subject>CATALYTIC EFFECTS</subject><subject>CHLORINATED AROMATIC HYDROCARBONS</subject><subject>DETOXIFICATION</subject><subject>ENERGY CONSERVATION, CONSUMPTION, AND UTILIZATION</subject><subject>ENVIRONMENTAL SCIENCES</subject><subject>Exact sciences and technology</subject><subject>General purification processes</subject><subject>HYDROGENATION</subject><subject>MATHEMATICAL MODELS</subject><subject>Pollution</subject><subject>REGENERATION</subject><subject>RUTHENIUM</subject><subject>WASTE WATER</subject><subject>Wastewaters</subject><subject>Water treatment and pollution</subject><issn>0888-5885</issn><issn>1520-5045</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>1999</creationdate><recordtype>article</recordtype><recordid>eNptkc9u1DAQxiMEEkvhwBtY4o_EIWAncexwq0ILRVuo6KIercGZUJesHTxesb1x5cYz8iR4tVW54Islz2---fxNUTwW_KXglXjlsOs4b_R8p1gIWfFS8kbeLRZca11KreX94gHRFedcyqZZFL9XlxGxPE84sx4STNfJWfYGU9i60VlILnh2FoNFIhZGdgGU8AckjKwPPoHzzn9l_eUUovP5eWCHMaxhJ9KH9Rw2fqDXf37-YkfbGaNbY-6Z2CekzZSIgR_YaRhw2omcEG2QHhb3RpgIH93cB8Xn46NV_65cfnx70h8uS2gqkcpBN53mshZjKwbdtlYpK_Jpui8grFCDzPWxGrkEBWht3aIApYYKamigVvVB8WSvGyg5Q9YltJc2eI82mSrnU2ulM_V8T80xfM_uklk7sjhN4DFsyAjV6mxiJ_diD9oYiCKOZs6_hXhtBDe7zZjbzWT26Y0okIVpjOCto38NXSd0JzJW7jGXI9_eliF-M62qlTSrs3Pzfnn6QR-vLszOwrM9D5bMVdhEn_P7z_i_MAeroQ</recordid><startdate>19991101</startdate><enddate>19991101</enddate><creator>Felis, Vincent</creator><creator>Fouilloux, Pierre</creator><creator>De Bellefon, Claude</creator><creator>Schweich, Daniel</creator><general>American Chemical Society</general><scope>BSCLL</scope><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7QH</scope><scope>OTOTI</scope></search><sort><creationdate>19991101</creationdate><title>Three-Step Catalytic Detoxification Process of Wastewater Containing Chlorinated Aromatic Compounds: Experimental Results and Modeling Issues</title><author>Felis, Vincent ; Fouilloux, Pierre ; De Bellefon, Claude ; Schweich, Daniel</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-a421t-d84980531f61d866c77c111149ba1c17d5498f2f05a7aecc36e1a77d2a3a4a373</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>1999</creationdate><topic>ACTIVATED CARBON</topic><topic>ADSORPTION</topic><topic>Applied sciences</topic><topic>CATALYTIC EFFECTS</topic><topic>CHLORINATED AROMATIC HYDROCARBONS</topic><topic>DETOXIFICATION</topic><topic>ENERGY CONSERVATION, CONSUMPTION, AND UTILIZATION</topic><topic>ENVIRONMENTAL SCIENCES</topic><topic>Exact sciences and technology</topic><topic>General purification processes</topic><topic>HYDROGENATION</topic><topic>MATHEMATICAL MODELS</topic><topic>Pollution</topic><topic>REGENERATION</topic><topic>RUTHENIUM</topic><topic>WASTE WATER</topic><topic>Wastewaters</topic><topic>Water treatment and pollution</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Felis, Vincent</creatorcontrib><creatorcontrib>Fouilloux, Pierre</creatorcontrib><creatorcontrib>De Bellefon, Claude</creatorcontrib><creatorcontrib>Schweich, Daniel</creatorcontrib><creatorcontrib>Lab. de Genie des Procedes Catalytiques, Villeurbanne (FR)</creatorcontrib><collection>Istex</collection><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Aqualine</collection><collection>OSTI.GOV</collection><jtitle>Industrial & engineering chemistry research</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Felis, Vincent</au><au>Fouilloux, Pierre</au><au>De Bellefon, Claude</au><au>Schweich, Daniel</au><aucorp>Lab. de Genie des Procedes Catalytiques, Villeurbanne (FR)</aucorp><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Three-Step Catalytic Detoxification Process of Wastewater Containing Chlorinated Aromatic Compounds: Experimental Results and Modeling Issues</atitle><jtitle>Industrial & engineering chemistry research</jtitle><addtitle>Ind. Eng. Chem. Res</addtitle><date>1999-11-01</date><risdate>1999</risdate><volume>38</volume><issue>11</issue><spage>4213</spage><epage>4219</epage><pages>4213-4219</pages><issn>0888-5885</issn><eissn>1520-5045</eissn><coden>IECRED</coden><abstract>Detoxification of water containing chlorinated aromatic compounds is performed in a single fixed bed using a periodic sequence of three steps: transient adsorption, catalytic hydrogenation, and thermal regeneration. The solid is both the adsorbent (activated carbon) and the catalyst (2.6% ruthenium loading). For chlorophenols, the end products are cyclohexanol and sodium chloride diluted in less than 2% of the amount of processed water. Adsorption is the critical step. The whole breakthrough curve is easily modeled. Conversely, the model fails to describe the early beginning which governs the purity of the effluent. The reaction step is performed under mild conditions (T < 353 K, P < 0.4 MPa) and is governed by the transient desorption of the pollutant, the catalytic reaction, and the mass-transfer processes. Thermal regeneration under hydrogen flow restores the adsorbent capacity and catalytic activity.</abstract><cop>Washington, DC</cop><pub>American Chemical Society</pub><doi>10.1021/ie990048p</doi><tpages>7</tpages></addata></record> |
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subjects | ACTIVATED CARBON ADSORPTION Applied sciences CATALYTIC EFFECTS CHLORINATED AROMATIC HYDROCARBONS DETOXIFICATION ENERGY CONSERVATION, CONSUMPTION, AND UTILIZATION ENVIRONMENTAL SCIENCES Exact sciences and technology General purification processes HYDROGENATION MATHEMATICAL MODELS Pollution REGENERATION RUTHENIUM WASTE WATER Wastewaters Water treatment and pollution |
title | Three-Step Catalytic Detoxification Process of Wastewater Containing Chlorinated Aromatic Compounds: Experimental Results and Modeling Issues |
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