Combining Ozonation and Ceramic Membrane Filtration for Tertiary Treatment
A pilot plant with a full scale monolithic ceramic membrane was operated at Ruhleben wastewater treatment plant (WWTP), Berlin Germany, for more than 12 months. Filtration performance according to the applied pre‐treatment (dose of ozone and coagulant) were investigated. Trial runs with and without...
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| Veröffentlicht in: | Chemie ingenieur technik 2013-08, Vol.85 (8), p.1237-1242 |
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| creator | Stüber, Johan Miehe, Ulf Stein, Robert Köhler, Mirco Lesjean, Boris |
| description | A pilot plant with a full scale monolithic ceramic membrane was operated at Ruhleben wastewater treatment plant (WWTP), Berlin Germany, for more than 12 months. Filtration performance according to the applied pre‐treatment (dose of ozone and coagulant) were investigated. Trial runs with and without ozone, varying the operational parameters such as flux, coagulant dosage, and filtration time were conducted in order to identify the benefits of pre‐ozonation. The reduction of the total fouling rate by ∼70 % when applying a specific ozone dose between 1.0 and 1.4 mg O 3 mgDOC–1 highlights the potential of ozonation as pre‐treatment step. Using LC‐OCD measurements, the effect of ozone on the biopolymer concentration and the DOC fraction was demonstrated.
Ozonation of secondary effluent is expected to be a promising pre‐treatment step to improve downstream membrane filtration. A pilot scale ceramic membrane module was operated with ozonation and coagulation in order to evaluate the potential of such a process setup. LC‐OCD measurements were conducted displaying the effect of the pre‐treatment stages. |
| doi_str_mv | 10.1002/cite.201200195 |
| format | Article |
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Ozonation of secondary effluent is expected to be a promising pre‐treatment step to improve downstream membrane filtration. A pilot scale ceramic membrane module was operated with ozonation and coagulation in order to evaluate the potential of such a process setup. LC‐OCD measurements were conducted displaying the effect of the pre‐treatment stages.</description><identifier>ISSN: 0009-286X</identifier><identifier>EISSN: 1522-2640</identifier><identifier>DOI: 10.1002/cite.201200195</identifier><language>eng</language><publisher>Weinheim: WILEY-VCH Verlag</publisher><subject>Ceramic membrane ; Ceramics ; Coagulants ; Dosage ; Effluents ; Filtration ; Fouling control ; Membranes ; Ozonation ; Ozone ; Pilots ; Tertiary treatment</subject><ispartof>Chemie ingenieur technik, 2013-08, Vol.85 (8), p.1237-1242</ispartof><rights>Copyright © 2013 WILEY‐VCH Verlag GmbH & Co. KGaA, Weinheim</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c3975-e77e5489635299a40eb06d4780005ff3a5ade1cf629a4049f2b070079f6a81783</citedby><cites>FETCH-LOGICAL-c3975-e77e5489635299a40eb06d4780005ff3a5ade1cf629a4049f2b070079f6a81783</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://onlinelibrary.wiley.com/doi/pdf/10.1002%2Fcite.201200195$$EPDF$$P50$$Gwiley$$H</linktopdf><linktohtml>$$Uhttps://onlinelibrary.wiley.com/doi/full/10.1002%2Fcite.201200195$$EHTML$$P50$$Gwiley$$H</linktohtml><link.rule.ids>314,780,784,1417,27924,27925,45574,45575</link.rule.ids></links><search><creatorcontrib>Stüber, Johan</creatorcontrib><creatorcontrib>Miehe, Ulf</creatorcontrib><creatorcontrib>Stein, Robert</creatorcontrib><creatorcontrib>Köhler, Mirco</creatorcontrib><creatorcontrib>Lesjean, Boris</creatorcontrib><title>Combining Ozonation and Ceramic Membrane Filtration for Tertiary Treatment</title><title>Chemie ingenieur technik</title><addtitle>Chemie Ingenieur Technik</addtitle><description>A pilot plant with a full scale monolithic ceramic membrane was operated at Ruhleben wastewater treatment plant (WWTP), Berlin Germany, for more than 12 months. Filtration performance according to the applied pre‐treatment (dose of ozone and coagulant) were investigated. Trial runs with and without ozone, varying the operational parameters such as flux, coagulant dosage, and filtration time were conducted in order to identify the benefits of pre‐ozonation. The reduction of the total fouling rate by ∼70 % when applying a specific ozone dose between 1.0 and 1.4 mg O 3 mgDOC–1 highlights the potential of ozonation as pre‐treatment step. Using LC‐OCD measurements, the effect of ozone on the biopolymer concentration and the DOC fraction was demonstrated.
Ozonation of secondary effluent is expected to be a promising pre‐treatment step to improve downstream membrane filtration. A pilot scale ceramic membrane module was operated with ozonation and coagulation in order to evaluate the potential of such a process setup. LC‐OCD measurements were conducted displaying the effect of the pre‐treatment stages.</description><subject>Ceramic membrane</subject><subject>Ceramics</subject><subject>Coagulants</subject><subject>Dosage</subject><subject>Effluents</subject><subject>Filtration</subject><subject>Fouling control</subject><subject>Membranes</subject><subject>Ozonation</subject><subject>Ozone</subject><subject>Pilots</subject><subject>Tertiary treatment</subject><issn>0009-286X</issn><issn>1522-2640</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2013</creationdate><recordtype>article</recordtype><recordid>eNqFkEtPwzAQhC0EEqVw5Zwjl5S1E8f2EUVtKRTKozxulptukCEPsFNB-fWkCqq4cVqtZr7d0RByTGFAAdhpZhscMKAMgCq-Q3qUMxayJIZd0gMAFTKZPO-TA-9f21W2co9cpHW5sJWtXoLZd12ZxtZVYKplkKIzpc2CKywXzlQYjGzRuE7PaxfM0TXWuHUwd2iaEqvmkOzlpvB49Dv75GE0nKfn4XQ2nqRn0zCLlOAhCoE8liqJOFPKxIALSJaxkG0mnueR4WaJNMsTthFjlbMFCACh8sRIKmTUJyfd3XdXf6zQN7q0PsOiaFPWK69p3P6RHKKotQ46a-Zq7x3m-t3Zsk2tKehNaXpTmt6W1gKqAz5tget_3DqdzId_2bBjrW_wa8sa96YTEQmun67H-vby_FHeyXt9E_0Av5J_NQ</recordid><startdate>201308</startdate><enddate>201308</enddate><creator>Stüber, Johan</creator><creator>Miehe, Ulf</creator><creator>Stein, Robert</creator><creator>Köhler, Mirco</creator><creator>Lesjean, Boris</creator><general>WILEY-VCH Verlag</general><general>WILEY‐VCH Verlag</general><scope>BSCLL</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7QQ</scope><scope>7U5</scope><scope>8FD</scope><scope>JG9</scope><scope>L7M</scope></search><sort><creationdate>201308</creationdate><title>Combining Ozonation and Ceramic Membrane Filtration for Tertiary Treatment</title><author>Stüber, Johan ; Miehe, Ulf ; Stein, Robert ; Köhler, Mirco ; Lesjean, Boris</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c3975-e77e5489635299a40eb06d4780005ff3a5ade1cf629a4049f2b070079f6a81783</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2013</creationdate><topic>Ceramic membrane</topic><topic>Ceramics</topic><topic>Coagulants</topic><topic>Dosage</topic><topic>Effluents</topic><topic>Filtration</topic><topic>Fouling control</topic><topic>Membranes</topic><topic>Ozonation</topic><topic>Ozone</topic><topic>Pilots</topic><topic>Tertiary treatment</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Stüber, Johan</creatorcontrib><creatorcontrib>Miehe, Ulf</creatorcontrib><creatorcontrib>Stein, Robert</creatorcontrib><creatorcontrib>Köhler, Mirco</creatorcontrib><creatorcontrib>Lesjean, Boris</creatorcontrib><collection>Istex</collection><collection>CrossRef</collection><collection>Ceramic Abstracts</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>Technology Research Database</collection><collection>Materials Research Database</collection><collection>Advanced Technologies Database with Aerospace</collection><jtitle>Chemie ingenieur technik</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Stüber, Johan</au><au>Miehe, Ulf</au><au>Stein, Robert</au><au>Köhler, Mirco</au><au>Lesjean, Boris</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Combining Ozonation and Ceramic Membrane Filtration for Tertiary Treatment</atitle><jtitle>Chemie ingenieur technik</jtitle><addtitle>Chemie Ingenieur Technik</addtitle><date>2013-08</date><risdate>2013</risdate><volume>85</volume><issue>8</issue><spage>1237</spage><epage>1242</epage><pages>1237-1242</pages><issn>0009-286X</issn><eissn>1522-2640</eissn><abstract>A pilot plant with a full scale monolithic ceramic membrane was operated at Ruhleben wastewater treatment plant (WWTP), Berlin Germany, for more than 12 months. Filtration performance according to the applied pre‐treatment (dose of ozone and coagulant) were investigated. Trial runs with and without ozone, varying the operational parameters such as flux, coagulant dosage, and filtration time were conducted in order to identify the benefits of pre‐ozonation. The reduction of the total fouling rate by ∼70 % when applying a specific ozone dose between 1.0 and 1.4 mg O 3 mgDOC–1 highlights the potential of ozonation as pre‐treatment step. Using LC‐OCD measurements, the effect of ozone on the biopolymer concentration and the DOC fraction was demonstrated.
Ozonation of secondary effluent is expected to be a promising pre‐treatment step to improve downstream membrane filtration. A pilot scale ceramic membrane module was operated with ozonation and coagulation in order to evaluate the potential of such a process setup. LC‐OCD measurements were conducted displaying the effect of the pre‐treatment stages.</abstract><cop>Weinheim</cop><pub>WILEY-VCH Verlag</pub><doi>10.1002/cite.201200195</doi><tpages>6</tpages></addata></record> |
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| subjects | Ceramic membrane Ceramics Coagulants Dosage Effluents Filtration Fouling control Membranes Ozonation Ozone Pilots Tertiary treatment |
| title | Combining Ozonation and Ceramic Membrane Filtration for Tertiary Treatment |
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