Treatment of primary settled municipal wastewater in a pilot scale MBR
Membrane bioreactors (MBRs) technology shows many advantages that convert it into an attractive solution for upgrading existent wastewater treatment plants (WWTP). The aim of this study was to investigate the feasibility of applying an MBR for treating primary settled wastewater in large WWTPs. In t...
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Veröffentlicht in: | Desalination and water treatment 2012-06, Vol.44 (1-3), p.197-204 |
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creator | IGLESIAS-OBELLEIRO, Angela FERNANDEZ-GONZALEZ, Roberto GARRIDO-FERNANDEZ, Juan Manuel |
description | Membrane bioreactors (MBRs) technology shows many advantages that convert it into an attractive solution for upgrading existent wastewater treatment plants (WWTP). The aim of this study was to investigate the feasibility of applying an MBR for treating primary settled wastewater in large WWTPs. In the 400,000 inhabitants equivalent WWTP of Vigo (NW Spain), 174,000 m3 d-1 of wastewater receives primary treatment, whereas only 130,000 m3 d-1 receives secondary treatment. In this facility, land scarcity is an issue, thus, the conventional activated sludge system (CAS) used may be replaced by MBR to retrofit this WWTP. This study was carried out in an MBR pilot plant of 3.97 m3 effective volume using a modified University of Cape Town (UCT) process with a Zenon ZW500d membrane module operating at low HRT (4-7 h). During the experimental stage, permeability values ranged from 90 to 125 l h-1 m-2 bar-1, with fluxes between 20-23 l m-2 h-1. Only three maintenance cleanings were applied during the 286 experimental days. Total COD values of the used wastewater were 50-350 mg l-1. Good performance in COD and BOD5 removal was achieved, being 15 ± 7 mg l-1 and 5 ± 3 mg l-1, respectively. Nitrogen removal efficiency was limited (40-60%), due to the low COD/N ratio in the influent. Primary settling protects MBR against membrane clogging and gives robustness to this technology. |
doi_str_mv | 10.1080/19443994.2012.691711 |
format | Article |
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The aim of this study was to investigate the feasibility of applying an MBR for treating primary settled wastewater in large WWTPs. In the 400,000 inhabitants equivalent WWTP of Vigo (NW Spain), 174,000 m3 d-1 of wastewater receives primary treatment, whereas only 130,000 m3 d-1 receives secondary treatment. In this facility, land scarcity is an issue, thus, the conventional activated sludge system (CAS) used may be replaced by MBR to retrofit this WWTP. This study was carried out in an MBR pilot plant of 3.97 m3 effective volume using a modified University of Cape Town (UCT) process with a Zenon ZW500d membrane module operating at low HRT (4-7 h). During the experimental stage, permeability values ranged from 90 to 125 l h-1 m-2 bar-1, with fluxes between 20-23 l m-2 h-1. Only three maintenance cleanings were applied during the 286 experimental days. Total COD values of the used wastewater were 50-350 mg l-1. Good performance in COD and BOD5 removal was achieved, being 15 ± 7 mg l-1 and 5 ± 3 mg l-1, respectively. Nitrogen removal efficiency was limited (40-60%), due to the low COD/N ratio in the influent. 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The aim of this study was to investigate the feasibility of applying an MBR for treating primary settled wastewater in large WWTPs. In the 400,000 inhabitants equivalent WWTP of Vigo (NW Spain), 174,000 m3 d-1 of wastewater receives primary treatment, whereas only 130,000 m3 d-1 receives secondary treatment. In this facility, land scarcity is an issue, thus, the conventional activated sludge system (CAS) used may be replaced by MBR to retrofit this WWTP. This study was carried out in an MBR pilot plant of 3.97 m3 effective volume using a modified University of Cape Town (UCT) process with a Zenon ZW500d membrane module operating at low HRT (4-7 h). During the experimental stage, permeability values ranged from 90 to 125 l h-1 m-2 bar-1, with fluxes between 20-23 l m-2 h-1. Only three maintenance cleanings were applied during the 286 experimental days. Total COD values of the used wastewater were 50-350 mg l-1. Good performance in COD and BOD5 removal was achieved, being 15 ± 7 mg l-1 and 5 ± 3 mg l-1, respectively. Nitrogen removal efficiency was limited (40-60%), due to the low COD/N ratio in the influent. Primary settling protects MBR against membrane clogging and gives robustness to this technology.</description><subject>Activated sludge</subject><subject>Applied sciences</subject><subject>Bioreactors</subject><subject>Exact sciences and technology</subject><subject>Municipal wastewater</subject><subject>Nitrogen removal</subject><subject>Pollution</subject><subject>Wastewater treatment plants</subject><subject>Water treatment and pollution</subject><issn>1944-3994</issn><issn>1944-3986</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2012</creationdate><recordtype>article</recordtype><recordid>eNo9UE1LAzEQDaJgqf0HHgLicWu-kzlqsVWoCFLPIc1mYct2d01Siv_eXVo7lxmG997MewjdUzKnxJAnCkJwADFnhLK5AqopvUKTcV1wMOr6MoO4RbOUdmQoKbQUbIKWmxhc3oc2467Cfaz3Lv7iFHJuQon3h7b2de8afHQph6PLIeK6xQ73ddNlnLxrAv54-bpDN5VrUpid-xR9L183i7di_bl6XzyvC8815MIrILqqTBlYuaVeyeHdUputkJpDAGmooVpxVXpPAmOebhkvwUnjiAQaOJ-ih5NuH7ufQ0jZ7rpDbIeTlhquCDeajShxQvnYpRRDZc_GLCV2DM3-h2bH0OwptIH2eBZ3o7EqutbX6cJl0oAAQ_gfq6RqZQ</recordid><startdate>20120601</startdate><enddate>20120601</enddate><creator>IGLESIAS-OBELLEIRO, Angela</creator><creator>FERNANDEZ-GONZALEZ, Roberto</creator><creator>GARRIDO-FERNANDEZ, Juan Manuel</creator><general>Desalination Publications</general><general>Elsevier Limited</general><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></search><sort><creationdate>20120601</creationdate><title>Treatment of primary settled municipal wastewater in a pilot scale MBR</title><author>IGLESIAS-OBELLEIRO, Angela ; FERNANDEZ-GONZALEZ, Roberto ; GARRIDO-FERNANDEZ, Juan Manuel</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c379t-c6907ff8de2db1c65691d78b45739e9581817636dcc0e22c1b23d9a58a0591e33</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2012</creationdate><topic>Activated sludge</topic><topic>Applied sciences</topic><topic>Bioreactors</topic><topic>Exact sciences and technology</topic><topic>Municipal wastewater</topic><topic>Nitrogen removal</topic><topic>Pollution</topic><topic>Wastewater treatment plants</topic><topic>Water treatment and pollution</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>IGLESIAS-OBELLEIRO, Angela</creatorcontrib><creatorcontrib>FERNANDEZ-GONZALEZ, Roberto</creatorcontrib><creatorcontrib>GARRIDO-FERNANDEZ, Juan Manuel</creatorcontrib><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><jtitle>Desalination and water treatment</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>IGLESIAS-OBELLEIRO, Angela</au><au>FERNANDEZ-GONZALEZ, Roberto</au><au>GARRIDO-FERNANDEZ, Juan Manuel</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Treatment of primary settled municipal wastewater in a pilot scale MBR</atitle><jtitle>Desalination and water treatment</jtitle><date>2012-06-01</date><risdate>2012</risdate><volume>44</volume><issue>1-3</issue><spage>197</spage><epage>204</epage><pages>197-204</pages><issn>1944-3994</issn><eissn>1944-3986</eissn><abstract>Membrane bioreactors (MBRs) technology shows many advantages that convert it into an attractive solution for upgrading existent wastewater treatment plants (WWTP). The aim of this study was to investigate the feasibility of applying an MBR for treating primary settled wastewater in large WWTPs. In the 400,000 inhabitants equivalent WWTP of Vigo (NW Spain), 174,000 m3 d-1 of wastewater receives primary treatment, whereas only 130,000 m3 d-1 receives secondary treatment. In this facility, land scarcity is an issue, thus, the conventional activated sludge system (CAS) used may be replaced by MBR to retrofit this WWTP. This study was carried out in an MBR pilot plant of 3.97 m3 effective volume using a modified University of Cape Town (UCT) process with a Zenon ZW500d membrane module operating at low HRT (4-7 h). During the experimental stage, permeability values ranged from 90 to 125 l h-1 m-2 bar-1, with fluxes between 20-23 l m-2 h-1. Only three maintenance cleanings were applied during the 286 experimental days. Total COD values of the used wastewater were 50-350 mg l-1. Good performance in COD and BOD5 removal was achieved, being 15 ± 7 mg l-1 and 5 ± 3 mg l-1, respectively. Nitrogen removal efficiency was limited (40-60%), due to the low COD/N ratio in the influent. Primary settling protects MBR against membrane clogging and gives robustness to this technology.</abstract><cop>L'Aquila</cop><pub>Desalination Publications</pub><doi>10.1080/19443994.2012.691711</doi><tpages>8</tpages></addata></record> |
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subjects | Activated sludge Applied sciences Bioreactors Exact sciences and technology Municipal wastewater Nitrogen removal Pollution Wastewater treatment plants Water treatment and pollution |
title | Treatment of primary settled municipal wastewater in a pilot scale MBR |
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