Performance of a flat-sheet submerged membrane bioreactor during long-term treatment of municipal wastewater
A pilot-scale submerged membrane bioreactor (SMBR) with anoxic and oxic tanks was operated in an attempt to reduce the problems concerning effective removal of organic matter and nutrients from municipal wastewater. A fl at type membrane with a pore size of 0.038μm and having a total surface area of...
Gespeichert in:
| Veröffentlicht in: | Desalination and water treatment 2011-02, Vol.26 (1-3), p.53-56 |
|---|---|
| Hauptverfasser: | , , , , , |
| Format: | Artikel |
| Sprache: | eng |
| Schlagworte: | |
| Online-Zugang: | Volltext |
| Tags: |
Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
|
| container_end_page | 56 |
|---|---|
| container_issue | 1-3 |
| container_start_page | 53 |
| container_title | Desalination and water treatment |
| container_volume | 26 |
| creator | Turan, Mustafa Ozdemir, Ozgur Turan, Abdullah Z. Ozkan, Oktay Bayhan, Hurrem Aykar, Erol |
| description | A pilot-scale submerged membrane bioreactor (SMBR) with anoxic and oxic tanks was operated in an attempt to reduce the problems concerning effective removal of organic matter and nutrients from municipal wastewater. A fl at type membrane with a pore size of 0.038μm and having a total surface area of 3.60 m2 was used in the experiments. During the operation, MLSS concentration in aeration (oxic) tank of SMBR was maintained at about 5–7 g/l. Influent and effluent pH in the SMBR also changed between 7.3–8.4. Raw wastewater with average chemical oxygen demand (COD): total nitrogen (TN) ratio of 12:2 was treated at various temperatures (10–30 °C) over an interval of about 160 d. When average influent nutrient mass ratio (COD:TN:TP) was 100:8.2:1.2 and BOD5:COD ratio was 0.5, removal efficiencies of COD, BOD5, TSS, TN and TP were 99.1%, 99.3%, 99.4%, 43.4% and 68.2%, respectively. Nitrification occurred in the aerobic reactor with NH4+–N removal efficiency ranging from 88.7 to 99.7% averaging at 97.8%. Nitrogen removal in the SMBR was limited not by nitrification but by denitrification. Increase in the concentration of TN in the treated water can be explained by increases in the concentration of NO3-–N. |
| doi_str_mv | 10.5004/dwt.2011.2109 |
| format | Article |
| fullrecord | <record><control><sourceid>proquest_cross</sourceid><recordid>TN_cdi_proquest_miscellaneous_872139261</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><els_id>S1944398624176102</els_id><sourcerecordid>872139261</sourcerecordid><originalsourceid>FETCH-LOGICAL-c478t-3a53c9ebcba4312be61228a4158286b6784d600f0af875d0ff5397237c179b7f3</originalsourceid><addsrcrecordid>eNp9kU1rFTEUhoeiYGm7dB8QqZu55mvysSzFtkJBF7oOmczJbcpkcptkvPjvzeWWIkLNJoHz5D2c83Tde4I3A8b887SvG4oJ2VCC9Ul3SjTnPdNKvPnr_a67KOURtzNwOXB62s3fIfuUo10coOSRRX62tS8PABWVdYyQtzChCHHMdgE0hpTBupoymtYcli2a07LtK-SIaqvUCEs9BMV1CS7s7Iz2tlTY24acd2-9nQtcPN9n3c-bLz-u7_r7b7dfr6_ue8elqj2zA3MaRjdazggdQRBKleVkUFSJUUjFJ4Gxx9YrOUzY-4FpSZl0ROpRenbWXR5zdzk9rVCqiaE4mOc2QVqLUZISpqkgjfz0X5IITqngXKuGfvgHfUxrXtochmjGsaCE00b1R8rlVEoGb3Y5RJt_G4LNQZRposxBlDmIavzH51RbnJ19W7IL5eUT5YQMXIjGySMHbW-_AmRTXIAmbQoZXDVTCq90-AOOuKWm</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>1934062142</pqid></control><display><type>article</type><title>Performance of a flat-sheet submerged membrane bioreactor during long-term treatment of municipal wastewater</title><source>Alma/SFX Local Collection</source><creator>Turan, Mustafa ; Ozdemir, Ozgur ; Turan, Abdullah Z. ; Ozkan, Oktay ; Bayhan, Hurrem ; Aykar, Erol</creator><creatorcontrib>Turan, Mustafa ; Ozdemir, Ozgur ; Turan, Abdullah Z. ; Ozkan, Oktay ; Bayhan, Hurrem ; Aykar, Erol</creatorcontrib><description>A pilot-scale submerged membrane bioreactor (SMBR) with anoxic and oxic tanks was operated in an attempt to reduce the problems concerning effective removal of organic matter and nutrients from municipal wastewater. A fl at type membrane with a pore size of 0.038μm and having a total surface area of 3.60 m2 was used in the experiments. During the operation, MLSS concentration in aeration (oxic) tank of SMBR was maintained at about 5–7 g/l. Influent and effluent pH in the SMBR also changed between 7.3–8.4. Raw wastewater with average chemical oxygen demand (COD): total nitrogen (TN) ratio of 12:2 was treated at various temperatures (10–30 °C) over an interval of about 160 d. When average influent nutrient mass ratio (COD:TN:TP) was 100:8.2:1.2 and BOD5:COD ratio was 0.5, removal efficiencies of COD, BOD5, TSS, TN and TP were 99.1%, 99.3%, 99.4%, 43.4% and 68.2%, respectively. Nitrification occurred in the aerobic reactor with NH4+–N removal efficiency ranging from 88.7 to 99.7% averaging at 97.8%. Nitrogen removal in the SMBR was limited not by nitrification but by denitrification. Increase in the concentration of TN in the treated water can be explained by increases in the concentration of NO3-–N.</description><identifier>ISSN: 1944-3986</identifier><identifier>ISSN: 1944-3994</identifier><identifier>EISSN: 1944-3986</identifier><identifier>DOI: 10.5004/dwt.2011.2109</identifier><language>eng</language><publisher>L'Aquila: Elsevier Inc</publisher><subject>Above ground tanks ; Aeration ; Aeration tanks ; Anoxia ; Applied sciences ; Bioreactors ; Chemical oxygen demand ; COD ; Crack opening displacement ; Denitrification ; Drinking water and swimming-pool water. Desalination ; Exact sciences and technology ; Influents ; Membranes ; Mineral nutrients ; Municipal wastewater ; Nitrification ; Nitrogen removal ; Nutrients ; Organic matter ; pH effects ; Pilot scale SMBR ; Pollution ; Pore size ; Porosity ; Raw wastewater ; Removal ; Tanks ; Total nitrogen ; Total phosphorus ; Treated water ; Waste water ; Wastewater ; Wastewater treatment ; Water treatment and pollution</subject><ispartof>Desalination and water treatment, 2011-02, Vol.26 (1-3), p.53-56</ispartof><rights>2011 Elsevier Inc.</rights><rights>2015 INIST-CNRS</rights><rights>Copyright Taylor & Francis Group, LLC</rights><lds50>peer_reviewed</lds50><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c478t-3a53c9ebcba4312be61228a4158286b6784d600f0af875d0ff5397237c179b7f3</citedby><cites>FETCH-LOGICAL-c478t-3a53c9ebcba4312be61228a4158286b6784d600f0af875d0ff5397237c179b7f3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>309,310,314,776,780,785,786,23911,23912,25120,27903,27904</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=24115466$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Turan, Mustafa</creatorcontrib><creatorcontrib>Ozdemir, Ozgur</creatorcontrib><creatorcontrib>Turan, Abdullah Z.</creatorcontrib><creatorcontrib>Ozkan, Oktay</creatorcontrib><creatorcontrib>Bayhan, Hurrem</creatorcontrib><creatorcontrib>Aykar, Erol</creatorcontrib><title>Performance of a flat-sheet submerged membrane bioreactor during long-term treatment of municipal wastewater</title><title>Desalination and water treatment</title><description>A pilot-scale submerged membrane bioreactor (SMBR) with anoxic and oxic tanks was operated in an attempt to reduce the problems concerning effective removal of organic matter and nutrients from municipal wastewater. A fl at type membrane with a pore size of 0.038μm and having a total surface area of 3.60 m2 was used in the experiments. During the operation, MLSS concentration in aeration (oxic) tank of SMBR was maintained at about 5–7 g/l. Influent and effluent pH in the SMBR also changed between 7.3–8.4. Raw wastewater with average chemical oxygen demand (COD): total nitrogen (TN) ratio of 12:2 was treated at various temperatures (10–30 °C) over an interval of about 160 d. When average influent nutrient mass ratio (COD:TN:TP) was 100:8.2:1.2 and BOD5:COD ratio was 0.5, removal efficiencies of COD, BOD5, TSS, TN and TP were 99.1%, 99.3%, 99.4%, 43.4% and 68.2%, respectively. Nitrification occurred in the aerobic reactor with NH4+–N removal efficiency ranging from 88.7 to 99.7% averaging at 97.8%. Nitrogen removal in the SMBR was limited not by nitrification but by denitrification. Increase in the concentration of TN in the treated water can be explained by increases in the concentration of NO3-–N.</description><subject>Above ground tanks</subject><subject>Aeration</subject><subject>Aeration tanks</subject><subject>Anoxia</subject><subject>Applied sciences</subject><subject>Bioreactors</subject><subject>Chemical oxygen demand</subject><subject>COD</subject><subject>Crack opening displacement</subject><subject>Denitrification</subject><subject>Drinking water and swimming-pool water. Desalination</subject><subject>Exact sciences and technology</subject><subject>Influents</subject><subject>Membranes</subject><subject>Mineral nutrients</subject><subject>Municipal wastewater</subject><subject>Nitrification</subject><subject>Nitrogen removal</subject><subject>Nutrients</subject><subject>Organic matter</subject><subject>pH effects</subject><subject>Pilot scale SMBR</subject><subject>Pollution</subject><subject>Pore size</subject><subject>Porosity</subject><subject>Raw wastewater</subject><subject>Removal</subject><subject>Tanks</subject><subject>Total nitrogen</subject><subject>Total phosphorus</subject><subject>Treated water</subject><subject>Waste water</subject><subject>Wastewater</subject><subject>Wastewater treatment</subject><subject>Water treatment and pollution</subject><issn>1944-3986</issn><issn>1944-3994</issn><issn>1944-3986</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2011</creationdate><recordtype>article</recordtype><recordid>eNp9kU1rFTEUhoeiYGm7dB8QqZu55mvysSzFtkJBF7oOmczJbcpkcptkvPjvzeWWIkLNJoHz5D2c83Tde4I3A8b887SvG4oJ2VCC9Ul3SjTnPdNKvPnr_a67KOURtzNwOXB62s3fIfuUo10coOSRRX62tS8PABWVdYyQtzChCHHMdgE0hpTBupoymtYcli2a07LtK-SIaqvUCEs9BMV1CS7s7Iz2tlTY24acd2-9nQtcPN9n3c-bLz-u7_r7b7dfr6_ue8elqj2zA3MaRjdazggdQRBKleVkUFSJUUjFJ4Gxx9YrOUzY-4FpSZl0ROpRenbWXR5zdzk9rVCqiaE4mOc2QVqLUZISpqkgjfz0X5IITqngXKuGfvgHfUxrXtochmjGsaCE00b1R8rlVEoGb3Y5RJt_G4LNQZRposxBlDmIavzH51RbnJ19W7IL5eUT5YQMXIjGySMHbW-_AmRTXIAmbQoZXDVTCq90-AOOuKWm</recordid><startdate>20110201</startdate><enddate>20110201</enddate><creator>Turan, Mustafa</creator><creator>Ozdemir, Ozgur</creator><creator>Turan, Abdullah Z.</creator><creator>Ozkan, Oktay</creator><creator>Bayhan, Hurrem</creator><creator>Aykar, Erol</creator><general>Elsevier Inc</general><general>Desalination Publications</general><general>Elsevier Limited</general><scope>6I.</scope><scope>AAFTH</scope><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7QH</scope><scope>7QL</scope><scope>7QO</scope><scope>7ST</scope><scope>7T7</scope><scope>7TN</scope><scope>7UA</scope><scope>8FD</scope><scope>C1K</scope><scope>F1W</scope><scope>FR3</scope><scope>H96</scope><scope>H97</scope><scope>KR7</scope><scope>L.G</scope><scope>M7N</scope><scope>P64</scope><scope>SOI</scope><scope>7SU</scope></search><sort><creationdate>20110201</creationdate><title>Performance of a flat-sheet submerged membrane bioreactor during long-term treatment of municipal wastewater</title><author>Turan, Mustafa ; Ozdemir, Ozgur ; Turan, Abdullah Z. ; Ozkan, Oktay ; Bayhan, Hurrem ; Aykar, Erol</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c478t-3a53c9ebcba4312be61228a4158286b6784d600f0af875d0ff5397237c179b7f3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2011</creationdate><topic>Above ground tanks</topic><topic>Aeration</topic><topic>Aeration tanks</topic><topic>Anoxia</topic><topic>Applied sciences</topic><topic>Bioreactors</topic><topic>Chemical oxygen demand</topic><topic>COD</topic><topic>Crack opening displacement</topic><topic>Denitrification</topic><topic>Drinking water and swimming-pool water. Desalination</topic><topic>Exact sciences and technology</topic><topic>Influents</topic><topic>Membranes</topic><topic>Mineral nutrients</topic><topic>Municipal wastewater</topic><topic>Nitrification</topic><topic>Nitrogen removal</topic><topic>Nutrients</topic><topic>Organic matter</topic><topic>pH effects</topic><topic>Pilot scale SMBR</topic><topic>Pollution</topic><topic>Pore size</topic><topic>Porosity</topic><topic>Raw wastewater</topic><topic>Removal</topic><topic>Tanks</topic><topic>Total nitrogen</topic><topic>Total phosphorus</topic><topic>Treated water</topic><topic>Waste water</topic><topic>Wastewater</topic><topic>Wastewater treatment</topic><topic>Water treatment and pollution</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Turan, Mustafa</creatorcontrib><creatorcontrib>Ozdemir, Ozgur</creatorcontrib><creatorcontrib>Turan, Abdullah Z.</creatorcontrib><creatorcontrib>Ozkan, Oktay</creatorcontrib><creatorcontrib>Bayhan, Hurrem</creatorcontrib><creatorcontrib>Aykar, Erol</creatorcontrib><collection>ScienceDirect Open Access Titles</collection><collection>Elsevier:ScienceDirect:Open Access</collection><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Aqualine</collection><collection>Bacteriology Abstracts (Microbiology B)</collection><collection>Biotechnology Research Abstracts</collection><collection>Environment Abstracts</collection><collection>Industrial and Applied Microbiology Abstracts (Microbiology A)</collection><collection>Oceanic Abstracts</collection><collection>Water Resources Abstracts</collection><collection>Technology Research Database</collection><collection>Environmental Sciences and Pollution Management</collection><collection>ASFA: Aquatic Sciences and Fisheries Abstracts</collection><collection>Engineering Research Database</collection><collection>Aquatic Science & Fisheries Abstracts (ASFA) 2: Ocean Technology, Policy & Non-Living Resources</collection><collection>Aquatic Science & Fisheries Abstracts (ASFA) 3: Aquatic Pollution & Environmental Quality</collection><collection>Civil Engineering Abstracts</collection><collection>Aquatic Science & Fisheries Abstracts (ASFA) Professional</collection><collection>Algology Mycology and Protozoology Abstracts (Microbiology C)</collection><collection>Biotechnology and BioEngineering Abstracts</collection><collection>Environment Abstracts</collection><collection>Environmental Engineering Abstracts</collection><jtitle>Desalination and water treatment</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Turan, Mustafa</au><au>Ozdemir, Ozgur</au><au>Turan, Abdullah Z.</au><au>Ozkan, Oktay</au><au>Bayhan, Hurrem</au><au>Aykar, Erol</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Performance of a flat-sheet submerged membrane bioreactor during long-term treatment of municipal wastewater</atitle><jtitle>Desalination and water treatment</jtitle><date>2011-02-01</date><risdate>2011</risdate><volume>26</volume><issue>1-3</issue><spage>53</spage><epage>56</epage><pages>53-56</pages><issn>1944-3986</issn><issn>1944-3994</issn><eissn>1944-3986</eissn><abstract>A pilot-scale submerged membrane bioreactor (SMBR) with anoxic and oxic tanks was operated in an attempt to reduce the problems concerning effective removal of organic matter and nutrients from municipal wastewater. A fl at type membrane with a pore size of 0.038μm and having a total surface area of 3.60 m2 was used in the experiments. During the operation, MLSS concentration in aeration (oxic) tank of SMBR was maintained at about 5–7 g/l. Influent and effluent pH in the SMBR also changed between 7.3–8.4. Raw wastewater with average chemical oxygen demand (COD): total nitrogen (TN) ratio of 12:2 was treated at various temperatures (10–30 °C) over an interval of about 160 d. When average influent nutrient mass ratio (COD:TN:TP) was 100:8.2:1.2 and BOD5:COD ratio was 0.5, removal efficiencies of COD, BOD5, TSS, TN and TP were 99.1%, 99.3%, 99.4%, 43.4% and 68.2%, respectively. Nitrification occurred in the aerobic reactor with NH4+–N removal efficiency ranging from 88.7 to 99.7% averaging at 97.8%. Nitrogen removal in the SMBR was limited not by nitrification but by denitrification. Increase in the concentration of TN in the treated water can be explained by increases in the concentration of NO3-–N.</abstract><cop>L'Aquila</cop><pub>Elsevier Inc</pub><doi>10.5004/dwt.2011.2109</doi><tpages>4</tpages><oa>free_for_read</oa></addata></record> |
| fulltext | fulltext |
| identifier | ISSN: 1944-3986 |
| ispartof | Desalination and water treatment, 2011-02, Vol.26 (1-3), p.53-56 |
| issn | 1944-3986 1944-3994 1944-3986 |
| language | eng |
| recordid | cdi_proquest_miscellaneous_872139261 |
| source | Alma/SFX Local Collection |
| subjects | Above ground tanks Aeration Aeration tanks Anoxia Applied sciences Bioreactors Chemical oxygen demand COD Crack opening displacement Denitrification Drinking water and swimming-pool water. Desalination Exact sciences and technology Influents Membranes Mineral nutrients Municipal wastewater Nitrification Nitrogen removal Nutrients Organic matter pH effects Pilot scale SMBR Pollution Pore size Porosity Raw wastewater Removal Tanks Total nitrogen Total phosphorus Treated water Waste water Wastewater Wastewater treatment Water treatment and pollution |
| title | Performance of a flat-sheet submerged membrane bioreactor during long-term treatment of municipal wastewater |
| url | https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-01-27T11%3A21%3A20IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-proquest_cross&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=Performance%20of%20a%20flat-sheet%20submerged%20membrane%20bioreactor%20during%20long-term%20treatment%20of%20municipal%20wastewater&rft.jtitle=Desalination%20and%20water%20treatment&rft.au=Turan,%20Mustafa&rft.date=2011-02-01&rft.volume=26&rft.issue=1-3&rft.spage=53&rft.epage=56&rft.pages=53-56&rft.issn=1944-3986&rft.eissn=1944-3986&rft_id=info:doi/10.5004/dwt.2011.2109&rft_dat=%3Cproquest_cross%3E872139261%3C/proquest_cross%3E%3Curl%3E%3C/url%3E&disable_directlink=true&sfx.directlink=off&sfx.report_link=0&rft_id=info:oai/&rft_pqid=1934062142&rft_id=info:pmid/&rft_els_id=S1944398624176102&rfr_iscdi=true |