Treatment of wastewater from dairy plants using Anaerobic Sequencing Batch Reactor (ASBR) following by Aerobic Sequencing Batch Reactor (SBR) aiming the removal of organic matter and nitrification
Studies on the environmental impacts of the food industry are important because the wastewater produced by these industries contains large amounts of organic matter and nutrients. Nitrogenous compounds released into the environment stimulate the greenhouse effect and threaten biodiversity. Sequencin...
Gespeichert in:
Veröffentlicht in: | Water practice and technology 2012-09, Vol.7 (3) |
---|---|
Hauptverfasser: | , , , , , |
Format: | Artikel |
Sprache: | eng |
Schlagworte: | |
Online-Zugang: | Volltext |
Tags: |
Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
|
container_end_page | |
---|---|
container_issue | 3 |
container_start_page | |
container_title | Water practice and technology |
container_volume | 7 |
creator | Matsumoto, E M Osako, M S Pinho, S C Tommaso, G Gomes, T M Ribeiro, R |
description | Studies on the environmental impacts of the food industry are important because the wastewater produced by these industries contains large amounts of organic matter and nutrients. Nitrogenous compounds released into the environment stimulate the greenhouse effect and threaten biodiversity. Sequencing batch reactors (SBR) have received a considerable amount of attention in recent years and have been used in the treatment of dairy wastewater in bench scale studies. Dairy plants are operated in batch regime and offer a good opportunity for wastewater treatment via sequential batch processes. Accordingly, the present article describes the results obtained in the first 100 days of operation of a system composed of an anaerobic sequencing batch (ASBR) followed by an aerobic reactor operated under SBR mode, for the treatment of wastewater generated by the USP Pirassununga dairy plant. SBR was used as post-treatment of ASBR to remove residual organic matter and to promote the nitrification of the effluent of the ASBR. Within a 24-h cycle, the ASBR removed 91.1 ± 5.0% of organic matter (chemical oxygen demand (COD) total). The initial concentration of total COD was approximately 4.5 g/L, and the organic loading rate was equal to 4.5 kg/m³ day. The SBR was operated for 24 h at a dissolved oxygen concentration of 3 mg/L, and NH4+-N was effectively converted to NO3−-N. At the end of the cycle, the concentration of NO3−-N and NO2−-N was equal to 26.0 ± 20.7 mg/L and 4.9 ± 2.97 mg/L, respectively. The SBR removed 75.5 ± 22.4% of the total total Kjeldahl nitrogen (TKN-N) of which 50% was converted to nitrate and 9% was converted to nitrite. It is believed that 41% of TKN-N removed may have been assimilated by microorganisms or converted to gaseous nitrogen by the denitrification during the stage of sedimentation. Moreover, phosphorus was also efficiently removed from the effluent, and the concentration of total phosphorous at the end of the cycle was equal to 4.9 ± 0.8 mg/L. Regarding the employment of the effluents from reactors for agricultural reuse, it was not observed sodification risk of soil; however the high values of electrical conductivity indicated a high potential for soil salinization. |
doi_str_mv | 10.2166/wpt.2012.048 |
format | Article |
fullrecord | <record><control><sourceid>proquest_cross</sourceid><recordid>TN_cdi_proquest_miscellaneous_1434015388</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>1943870449</sourcerecordid><originalsourceid>FETCH-LOGICAL-c296t-e2d23a14da99215846fb2df3907e6a3e524ddad911309c6befa9f03229a365213</originalsourceid><addsrcrecordid>eNqFUctKBDEQHETB580PCHhRcNe8ZnZyXMUXCIIP8BZ6Mx2NzCRrknXZ__PDnFEP4sVTN11VTXVXUewzOuasqk6W8zzmlPExlfVascUmJRtxwZ7Wf_WbxXZKr5RWE1WLreLjISLkDn0mwZIlpIxLyBiJjaEjDbi4IvMWfE5kkZx_JlMPGMPMGXKPbwv0ZhieQjYv5A7B5BDJ4fT-9O6I2NC2YTnAsxWZ_iv60oDrBii_IInYhXdoB1shPoPvxR3kwRr4hniXo7POQHbB7xYbFtqEez91p3i8OH84uxrd3F5en01vRoarKo-QN1wAkw0oxVlZy8rOeGOFohOsQGDJZdNAoxgTVJlqhhaUpYJzBaIqORM7xeH33nkM_Rkp684lg23_HwyLpJkUkrJS1HVPPfhDfQ2L6Ht3mikp6gmVUvWs42-WiSGliFbPo-sgrjSjeohU95HqIVLdRyo-AaTJlwg</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>1943870449</pqid></control><display><type>article</type><title>Treatment of wastewater from dairy plants using Anaerobic Sequencing Batch Reactor (ASBR) following by Aerobic Sequencing Batch Reactor (SBR) aiming the removal of organic matter and nitrification</title><source>EZB-FREE-00999 freely available EZB journals</source><creator>Matsumoto, E M ; Osako, M S ; Pinho, S C ; Tommaso, G ; Gomes, T M ; Ribeiro, R</creator><creatorcontrib>Matsumoto, E M ; Osako, M S ; Pinho, S C ; Tommaso, G ; Gomes, T M ; Ribeiro, R</creatorcontrib><description>Studies on the environmental impacts of the food industry are important because the wastewater produced by these industries contains large amounts of organic matter and nutrients. Nitrogenous compounds released into the environment stimulate the greenhouse effect and threaten biodiversity. Sequencing batch reactors (SBR) have received a considerable amount of attention in recent years and have been used in the treatment of dairy wastewater in bench scale studies. Dairy plants are operated in batch regime and offer a good opportunity for wastewater treatment via sequential batch processes. Accordingly, the present article describes the results obtained in the first 100 days of operation of a system composed of an anaerobic sequencing batch (ASBR) followed by an aerobic reactor operated under SBR mode, for the treatment of wastewater generated by the USP Pirassununga dairy plant. SBR was used as post-treatment of ASBR to remove residual organic matter and to promote the nitrification of the effluent of the ASBR. Within a 24-h cycle, the ASBR removed 91.1 ± 5.0% of organic matter (chemical oxygen demand (COD) total). The initial concentration of total COD was approximately 4.5 g/L, and the organic loading rate was equal to 4.5 kg/m³ day. The SBR was operated for 24 h at a dissolved oxygen concentration of 3 mg/L, and NH4+-N was effectively converted to NO3−-N. At the end of the cycle, the concentration of NO3−-N and NO2−-N was equal to 26.0 ± 20.7 mg/L and 4.9 ± 2.97 mg/L, respectively. The SBR removed 75.5 ± 22.4% of the total total Kjeldahl nitrogen (TKN-N) of which 50% was converted to nitrate and 9% was converted to nitrite. It is believed that 41% of TKN-N removed may have been assimilated by microorganisms or converted to gaseous nitrogen by the denitrification during the stage of sedimentation. Moreover, phosphorus was also efficiently removed from the effluent, and the concentration of total phosphorous at the end of the cycle was equal to 4.9 ± 0.8 mg/L. Regarding the employment of the effluents from reactors for agricultural reuse, it was not observed sodification risk of soil; however the high values of electrical conductivity indicated a high potential for soil salinization.</description><identifier>ISSN: 1751-231X</identifier><identifier>EISSN: 1751-231X</identifier><identifier>DOI: 10.2166/wpt.2012.048</identifier><language>eng</language><publisher>London: IWA Publishing</publisher><subject>Anaerobic treatment ; Batch processes ; Batch processing ; Batch reactors ; Biodiversity ; Bioreactors ; Chemical oxygen demand ; Dairy industry wastewaters ; Denitrification ; Dissolved oxygen ; Effluents ; Electrical conductivity ; Electrical resistivity ; Environmental impact ; Environmental studies ; Farm buildings ; Food industry ; Food processing industry ; Greenhouse effect ; Industry ; Load distribution ; Loading rate ; Microorganisms ; Mineral nutrients ; Nitrates ; Nitrification ; Nitrogen compounds ; Nitrogen dioxide ; Nutrients ; Organic loading ; Organic matter ; Phosphorus ; Plants (botany) ; Reactors ; Removal ; Salinization ; Sedimentation ; Sequences ; Sequencing ; Sequencing batch reactor ; Soil ; Soil salinity ; Soil salinization ; Wastewater ; Wastewater treatment ; Wastewater treatment plants</subject><ispartof>Water practice and technology, 2012-09, Vol.7 (3)</ispartof><rights>Copyright IWA Publishing Sep 2012</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c296t-e2d23a14da99215846fb2df3907e6a3e524ddad911309c6befa9f03229a365213</citedby></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,780,784,27923,27924</link.rule.ids></links><search><creatorcontrib>Matsumoto, E M</creatorcontrib><creatorcontrib>Osako, M S</creatorcontrib><creatorcontrib>Pinho, S C</creatorcontrib><creatorcontrib>Tommaso, G</creatorcontrib><creatorcontrib>Gomes, T M</creatorcontrib><creatorcontrib>Ribeiro, R</creatorcontrib><title>Treatment of wastewater from dairy plants using Anaerobic Sequencing Batch Reactor (ASBR) following by Aerobic Sequencing Batch Reactor (SBR) aiming the removal of organic matter and nitrification</title><title>Water practice and technology</title><description>Studies on the environmental impacts of the food industry are important because the wastewater produced by these industries contains large amounts of organic matter and nutrients. Nitrogenous compounds released into the environment stimulate the greenhouse effect and threaten biodiversity. Sequencing batch reactors (SBR) have received a considerable amount of attention in recent years and have been used in the treatment of dairy wastewater in bench scale studies. Dairy plants are operated in batch regime and offer a good opportunity for wastewater treatment via sequential batch processes. Accordingly, the present article describes the results obtained in the first 100 days of operation of a system composed of an anaerobic sequencing batch (ASBR) followed by an aerobic reactor operated under SBR mode, for the treatment of wastewater generated by the USP Pirassununga dairy plant. SBR was used as post-treatment of ASBR to remove residual organic matter and to promote the nitrification of the effluent of the ASBR. Within a 24-h cycle, the ASBR removed 91.1 ± 5.0% of organic matter (chemical oxygen demand (COD) total). The initial concentration of total COD was approximately 4.5 g/L, and the organic loading rate was equal to 4.5 kg/m³ day. The SBR was operated for 24 h at a dissolved oxygen concentration of 3 mg/L, and NH4+-N was effectively converted to NO3−-N. At the end of the cycle, the concentration of NO3−-N and NO2−-N was equal to 26.0 ± 20.7 mg/L and 4.9 ± 2.97 mg/L, respectively. The SBR removed 75.5 ± 22.4% of the total total Kjeldahl nitrogen (TKN-N) of which 50% was converted to nitrate and 9% was converted to nitrite. It is believed that 41% of TKN-N removed may have been assimilated by microorganisms or converted to gaseous nitrogen by the denitrification during the stage of sedimentation. Moreover, phosphorus was also efficiently removed from the effluent, and the concentration of total phosphorous at the end of the cycle was equal to 4.9 ± 0.8 mg/L. Regarding the employment of the effluents from reactors for agricultural reuse, it was not observed sodification risk of soil; however the high values of electrical conductivity indicated a high potential for soil salinization.</description><subject>Anaerobic treatment</subject><subject>Batch processes</subject><subject>Batch processing</subject><subject>Batch reactors</subject><subject>Biodiversity</subject><subject>Bioreactors</subject><subject>Chemical oxygen demand</subject><subject>Dairy industry wastewaters</subject><subject>Denitrification</subject><subject>Dissolved oxygen</subject><subject>Effluents</subject><subject>Electrical conductivity</subject><subject>Electrical resistivity</subject><subject>Environmental impact</subject><subject>Environmental studies</subject><subject>Farm buildings</subject><subject>Food industry</subject><subject>Food processing industry</subject><subject>Greenhouse effect</subject><subject>Industry</subject><subject>Load distribution</subject><subject>Loading rate</subject><subject>Microorganisms</subject><subject>Mineral nutrients</subject><subject>Nitrates</subject><subject>Nitrification</subject><subject>Nitrogen compounds</subject><subject>Nitrogen dioxide</subject><subject>Nutrients</subject><subject>Organic loading</subject><subject>Organic matter</subject><subject>Phosphorus</subject><subject>Plants (botany)</subject><subject>Reactors</subject><subject>Removal</subject><subject>Salinization</subject><subject>Sedimentation</subject><subject>Sequences</subject><subject>Sequencing</subject><subject>Sequencing batch reactor</subject><subject>Soil</subject><subject>Soil salinity</subject><subject>Soil salinization</subject><subject>Wastewater</subject><subject>Wastewater treatment</subject><subject>Wastewater treatment plants</subject><issn>1751-231X</issn><issn>1751-231X</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2012</creationdate><recordtype>article</recordtype><sourceid>AFKRA</sourceid><sourceid>AZQEC</sourceid><sourceid>BENPR</sourceid><sourceid>CCPQU</sourceid><sourceid>DWQXO</sourceid><sourceid>GNUQQ</sourceid><recordid>eNqFUctKBDEQHETB580PCHhRcNe8ZnZyXMUXCIIP8BZ6Mx2NzCRrknXZ__PDnFEP4sVTN11VTXVXUewzOuasqk6W8zzmlPExlfVascUmJRtxwZ7Wf_WbxXZKr5RWE1WLreLjISLkDn0mwZIlpIxLyBiJjaEjDbi4IvMWfE5kkZx_JlMPGMPMGXKPbwv0ZhieQjYv5A7B5BDJ4fT-9O6I2NC2YTnAsxWZ_iv60oDrBii_IInYhXdoB1shPoPvxR3kwRr4hniXo7POQHbB7xYbFtqEez91p3i8OH84uxrd3F5en01vRoarKo-QN1wAkw0oxVlZy8rOeGOFohOsQGDJZdNAoxgTVJlqhhaUpYJzBaIqORM7xeH33nkM_Rkp684lg23_HwyLpJkUkrJS1HVPPfhDfQ2L6Ht3mikp6gmVUvWs42-WiSGliFbPo-sgrjSjeohU95HqIVLdRyo-AaTJlwg</recordid><startdate>20120901</startdate><enddate>20120901</enddate><creator>Matsumoto, E M</creator><creator>Osako, M S</creator><creator>Pinho, S C</creator><creator>Tommaso, G</creator><creator>Gomes, T M</creator><creator>Ribeiro, R</creator><general>IWA Publishing</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7QH</scope><scope>7UA</scope><scope>AEUYN</scope><scope>AFKRA</scope><scope>ATCPS</scope><scope>AZQEC</scope><scope>BENPR</scope><scope>BHPHI</scope><scope>BKSAR</scope><scope>C1K</scope><scope>CCPQU</scope><scope>DWQXO</scope><scope>F1W</scope><scope>GNUQQ</scope><scope>H96</scope><scope>H97</scope><scope>HCIFZ</scope><scope>L.G</scope><scope>PATMY</scope><scope>PCBAR</scope><scope>PQEST</scope><scope>PQQKQ</scope><scope>PQUKI</scope><scope>PYCSY</scope><scope>7TV</scope></search><sort><creationdate>20120901</creationdate><title>Treatment of wastewater from dairy plants using Anaerobic Sequencing Batch Reactor (ASBR) following by Aerobic Sequencing Batch Reactor (SBR) aiming the removal of organic matter and nitrification</title><author>Matsumoto, E M ; Osako, M S ; Pinho, S C ; Tommaso, G ; Gomes, T M ; Ribeiro, R</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c296t-e2d23a14da99215846fb2df3907e6a3e524ddad911309c6befa9f03229a365213</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2012</creationdate><topic>Anaerobic treatment</topic><topic>Batch processes</topic><topic>Batch processing</topic><topic>Batch reactors</topic><topic>Biodiversity</topic><topic>Bioreactors</topic><topic>Chemical oxygen demand</topic><topic>Dairy industry wastewaters</topic><topic>Denitrification</topic><topic>Dissolved oxygen</topic><topic>Effluents</topic><topic>Electrical conductivity</topic><topic>Electrical resistivity</topic><topic>Environmental impact</topic><topic>Environmental studies</topic><topic>Farm buildings</topic><topic>Food industry</topic><topic>Food processing industry</topic><topic>Greenhouse effect</topic><topic>Industry</topic><topic>Load distribution</topic><topic>Loading rate</topic><topic>Microorganisms</topic><topic>Mineral nutrients</topic><topic>Nitrates</topic><topic>Nitrification</topic><topic>Nitrogen compounds</topic><topic>Nitrogen dioxide</topic><topic>Nutrients</topic><topic>Organic loading</topic><topic>Organic matter</topic><topic>Phosphorus</topic><topic>Plants (botany)</topic><topic>Reactors</topic><topic>Removal</topic><topic>Salinization</topic><topic>Sedimentation</topic><topic>Sequences</topic><topic>Sequencing</topic><topic>Sequencing batch reactor</topic><topic>Soil</topic><topic>Soil salinity</topic><topic>Soil salinization</topic><topic>Wastewater</topic><topic>Wastewater treatment</topic><topic>Wastewater treatment plants</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Matsumoto, E M</creatorcontrib><creatorcontrib>Osako, M S</creatorcontrib><creatorcontrib>Pinho, S C</creatorcontrib><creatorcontrib>Tommaso, G</creatorcontrib><creatorcontrib>Gomes, T M</creatorcontrib><creatorcontrib>Ribeiro, R</creatorcontrib><collection>CrossRef</collection><collection>Aqualine</collection><collection>Water Resources Abstracts</collection><collection>ProQuest One Sustainability</collection><collection>ProQuest Central UK/Ireland</collection><collection>Agricultural & Environmental Science Collection</collection><collection>ProQuest Central Essentials</collection><collection>ProQuest Central</collection><collection>Natural Science Collection</collection><collection>Earth, Atmospheric & Aquatic Science Collection</collection><collection>Environmental Sciences and Pollution Management</collection><collection>ProQuest One Community College</collection><collection>ProQuest Central Korea</collection><collection>ASFA: Aquatic Sciences and Fisheries Abstracts</collection><collection>ProQuest Central Student</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>SciTech Premium Collection</collection><collection>Aquatic Science & Fisheries Abstracts (ASFA) Professional</collection><collection>Environmental Science Database</collection><collection>Earth, Atmospheric & Aquatic Science Database</collection><collection>ProQuest One Academic Eastern Edition (DO NOT USE)</collection><collection>ProQuest One Academic</collection><collection>ProQuest One Academic UKI Edition</collection><collection>Environmental Science Collection</collection><collection>Pollution Abstracts</collection><jtitle>Water practice and technology</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Matsumoto, E M</au><au>Osako, M S</au><au>Pinho, S C</au><au>Tommaso, G</au><au>Gomes, T M</au><au>Ribeiro, R</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Treatment of wastewater from dairy plants using Anaerobic Sequencing Batch Reactor (ASBR) following by Aerobic Sequencing Batch Reactor (SBR) aiming the removal of organic matter and nitrification</atitle><jtitle>Water practice and technology</jtitle><date>2012-09-01</date><risdate>2012</risdate><volume>7</volume><issue>3</issue><issn>1751-231X</issn><eissn>1751-231X</eissn><abstract>Studies on the environmental impacts of the food industry are important because the wastewater produced by these industries contains large amounts of organic matter and nutrients. Nitrogenous compounds released into the environment stimulate the greenhouse effect and threaten biodiversity. Sequencing batch reactors (SBR) have received a considerable amount of attention in recent years and have been used in the treatment of dairy wastewater in bench scale studies. Dairy plants are operated in batch regime and offer a good opportunity for wastewater treatment via sequential batch processes. Accordingly, the present article describes the results obtained in the first 100 days of operation of a system composed of an anaerobic sequencing batch (ASBR) followed by an aerobic reactor operated under SBR mode, for the treatment of wastewater generated by the USP Pirassununga dairy plant. SBR was used as post-treatment of ASBR to remove residual organic matter and to promote the nitrification of the effluent of the ASBR. Within a 24-h cycle, the ASBR removed 91.1 ± 5.0% of organic matter (chemical oxygen demand (COD) total). The initial concentration of total COD was approximately 4.5 g/L, and the organic loading rate was equal to 4.5 kg/m³ day. The SBR was operated for 24 h at a dissolved oxygen concentration of 3 mg/L, and NH4+-N was effectively converted to NO3−-N. At the end of the cycle, the concentration of NO3−-N and NO2−-N was equal to 26.0 ± 20.7 mg/L and 4.9 ± 2.97 mg/L, respectively. The SBR removed 75.5 ± 22.4% of the total total Kjeldahl nitrogen (TKN-N) of which 50% was converted to nitrate and 9% was converted to nitrite. It is believed that 41% of TKN-N removed may have been assimilated by microorganisms or converted to gaseous nitrogen by the denitrification during the stage of sedimentation. Moreover, phosphorus was also efficiently removed from the effluent, and the concentration of total phosphorous at the end of the cycle was equal to 4.9 ± 0.8 mg/L. Regarding the employment of the effluents from reactors for agricultural reuse, it was not observed sodification risk of soil; however the high values of electrical conductivity indicated a high potential for soil salinization.</abstract><cop>London</cop><pub>IWA Publishing</pub><doi>10.2166/wpt.2012.048</doi></addata></record> |
fulltext | fulltext |
identifier | ISSN: 1751-231X |
ispartof | Water practice and technology, 2012-09, Vol.7 (3) |
issn | 1751-231X 1751-231X |
language | eng |
recordid | cdi_proquest_miscellaneous_1434015388 |
source | EZB-FREE-00999 freely available EZB journals |
subjects | Anaerobic treatment Batch processes Batch processing Batch reactors Biodiversity Bioreactors Chemical oxygen demand Dairy industry wastewaters Denitrification Dissolved oxygen Effluents Electrical conductivity Electrical resistivity Environmental impact Environmental studies Farm buildings Food industry Food processing industry Greenhouse effect Industry Load distribution Loading rate Microorganisms Mineral nutrients Nitrates Nitrification Nitrogen compounds Nitrogen dioxide Nutrients Organic loading Organic matter Phosphorus Plants (botany) Reactors Removal Salinization Sedimentation Sequences Sequencing Sequencing batch reactor Soil Soil salinity Soil salinization Wastewater Wastewater treatment Wastewater treatment plants |
title | Treatment of wastewater from dairy plants using Anaerobic Sequencing Batch Reactor (ASBR) following by Aerobic Sequencing Batch Reactor (SBR) aiming the removal of organic matter and nitrification |
url | https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-01-08T18%3A15%3A24IST&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=Treatment%20of%20wastewater%20from%20dairy%20plants%20using%20Anaerobic%20Sequencing%20Batch%20Reactor%20(ASBR)%20following%20by%20Aerobic%20Sequencing%20Batch%20Reactor%20(SBR)%20aiming%20the%20removal%20of%20organic%20matter%20and%20nitrification&rft.jtitle=Water%20practice%20and%20technology&rft.au=Matsumoto,%20E%20M&rft.date=2012-09-01&rft.volume=7&rft.issue=3&rft.issn=1751-231X&rft.eissn=1751-231X&rft_id=info:doi/10.2166/wpt.2012.048&rft_dat=%3Cproquest_cross%3E1943870449%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=1943870449&rft_id=info:pmid/&rfr_iscdi=true |