Loading…

Application of sequencing batch biofilm reactor (SBBR) in dairy wastewater treatment

Application of lab-scale sequencing batch (SBR) and sequencing batch biofilm reactors (SBBR) for treatment of dairy wastewater was investigated under organic loading of 1,130-1,560 gBOD 5 /m 3 ·d. The main characteristics of the dairy wastewater were: pH=4.9, chemical oxygen demand (COD)=16,264 mg/...

Full description

Saved in:
Bibliographic Details
Published in:The Korean journal of chemical engineering 2019, 36(2), 227, pp.248-254
Main Authors: Ozturk, Arzu, Aygun, Ahmet, Nas, Bilgehan
Format: Article
Language:English
Subjects:
Citations: Items that this one cites
Items that cite this one
Online Access:Get full text
Tags: Add Tag
No Tags, Be the first to tag this record!
cited_by cdi_FETCH-LOGICAL-c350t-ea8830a53ea354258c04195d29c1ea8fb0907d2fdc7a52ce48a916c340b7d9283
cites cdi_FETCH-LOGICAL-c350t-ea8830a53ea354258c04195d29c1ea8fb0907d2fdc7a52ce48a916c340b7d9283
container_end_page 254
container_issue 2
container_start_page 248
container_title The Korean journal of chemical engineering
container_volume 36
creator Ozturk, Arzu
Aygun, Ahmet
Nas, Bilgehan
description Application of lab-scale sequencing batch (SBR) and sequencing batch biofilm reactors (SBBR) for treatment of dairy wastewater was investigated under organic loading of 1,130-1,560 gBOD 5 /m 3 ·d. The main characteristics of the dairy wastewater were: pH=4.9, chemical oxygen demand (COD)=16,264 mg/ l ; biological oxygen demand (BOD 5 )=10,536 mg/ l , PO 4 -P=342 mg/ l ; total nitrogen (TN)=224 mg/ l . SBBR was filled with the Kaldnes K1 biocarrier at 30% of the volume of empty reactor. The SBR and SBBR were operated in fixed 24 h cycles, each consisting of 30 min fill up, 22 h aeration, 1.5 h settle, 30 min decant, and idle with a hydraulic retention time (HRT) of 8 days. Operational parameters such as pH, dissolved oxygen (DO), mixed liquor suspended solid (MLSS), solids retention time (SRT) and sludge volume index (SVI) were monitored during the whole cycle. The effects of these parameters on the COD, nitrogen and phosphorus removal were discussed in this paper. As a result, adding biocarrier to the reactor had a positive effect on organic with COD removal of 63.5% for SBR and 81.8% for SBBR and nutrient removal with ammonium removal of 66.0% for SBR and 85.1% for SBBR in treatment of dairy wastewater.
doi_str_mv 10.1007/s11814-018-0198-2
format article
fullrecord <record><control><sourceid>proquest_nrf_k</sourceid><recordid>TN_cdi_nrf_kci_oai_kci_go_kr_ARTI_4099098</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>2173836457</sourcerecordid><originalsourceid>FETCH-LOGICAL-c350t-ea8830a53ea354258c04195d29c1ea8fb0907d2fdc7a52ce48a916c340b7d9283</originalsourceid><addsrcrecordid>eNp1kEtLAzEUhYMoWKs_wF3AjV2M3mQmnWTZFh-FglDrOmQymZo-JjVJKf33po7gysXlLO53DvcehG4JPBCA8jEQwkmRAeFpBM_oGeoRUbKspBTOUQ8oG2aEEHaJrkJYATA2pNBDi9Fut7FaReta7BoczNfetNq2S1ypqD9xZV1jN1vsjdLReXz_Ph7PB9i2uFbWH_FBhWgOKhqPY2Li1rTxGl00ahPMza_20cfz02Lyms3eXqaT0SzTOYOYGcV5DorlRuWsoIxrKIhgNRWapF1TgYCypk2tS8WoNgVXggx1XkBV1oLyvI8GXW7rG7nWVjplf3Tp5NrL0XwxlQUIAeLE3nXszrv0Yohy5fa-TedJSsqc58OClYkiHaW9C8GbRu683Sp_lATkqWjZFS1T0fJUtKTJQztPSGy7NP4v-X_TN3YwfxI</addsrcrecordid><sourcetype>Open Website</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>2173836457</pqid></control><display><type>article</type><title>Application of sequencing batch biofilm reactor (SBBR) in dairy wastewater treatment</title><source>Springer Nature</source><creator>Ozturk, Arzu ; Aygun, Ahmet ; Nas, Bilgehan</creator><creatorcontrib>Ozturk, Arzu ; Aygun, Ahmet ; Nas, Bilgehan</creatorcontrib><description>Application of lab-scale sequencing batch (SBR) and sequencing batch biofilm reactors (SBBR) for treatment of dairy wastewater was investigated under organic loading of 1,130-1,560 gBOD 5 /m 3 ·d. The main characteristics of the dairy wastewater were: pH=4.9, chemical oxygen demand (COD)=16,264 mg/ l ; biological oxygen demand (BOD 5 )=10,536 mg/ l , PO 4 -P=342 mg/ l ; total nitrogen (TN)=224 mg/ l . SBBR was filled with the Kaldnes K1 biocarrier at 30% of the volume of empty reactor. The SBR and SBBR were operated in fixed 24 h cycles, each consisting of 30 min fill up, 22 h aeration, 1.5 h settle, 30 min decant, and idle with a hydraulic retention time (HRT) of 8 days. Operational parameters such as pH, dissolved oxygen (DO), mixed liquor suspended solid (MLSS), solids retention time (SRT) and sludge volume index (SVI) were monitored during the whole cycle. The effects of these parameters on the COD, nitrogen and phosphorus removal were discussed in this paper. As a result, adding biocarrier to the reactor had a positive effect on organic with COD removal of 63.5% for SBR and 81.8% for SBBR and nutrient removal with ammonium removal of 66.0% for SBR and 85.1% for SBBR in treatment of dairy wastewater.</description><identifier>ISSN: 0256-1115</identifier><identifier>EISSN: 1975-7220</identifier><identifier>DOI: 10.1007/s11814-018-0198-2</identifier><language>eng</language><publisher>New York: Springer US</publisher><subject>Aeration ; Biofilms ; Biotechnology ; Catalysis ; Chemical oxygen demand ; Chemistry ; Chemistry and Materials Science ; Decantation ; Environmental Engineering ; Hydraulic retention time ; Industrial Chemistry/Chemical Engineering ; Materials Science ; Organic chemistry ; Parameters ; Phosphorus removal ; Sludge ; Solid suspensions ; Wastewater treatment ; 화학공학</subject><ispartof>Korean Journal of Chemical Engineering, 2019, 36(2), 227, pp.248-254</ispartof><rights>Korean Institute of Chemical Engineers, Seoul, Korea 2019</rights><rights>Copyright Springer Nature B.V. 2019</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c350t-ea8830a53ea354258c04195d29c1ea8fb0907d2fdc7a52ce48a916c340b7d9283</citedby><cites>FETCH-LOGICAL-c350t-ea8830a53ea354258c04195d29c1ea8fb0907d2fdc7a52ce48a916c340b7d9283</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,780,784,27924,27925</link.rule.ids><backlink>$$Uhttps://www.kci.go.kr/kciportal/ci/sereArticleSearch/ciSereArtiView.kci?sereArticleSearchBean.artiId=ART002433465$$DAccess content in National Research Foundation of Korea (NRF)$$Hfree_for_read</backlink></links><search><creatorcontrib>Ozturk, Arzu</creatorcontrib><creatorcontrib>Aygun, Ahmet</creatorcontrib><creatorcontrib>Nas, Bilgehan</creatorcontrib><title>Application of sequencing batch biofilm reactor (SBBR) in dairy wastewater treatment</title><title>The Korean journal of chemical engineering</title><addtitle>Korean J. Chem. Eng</addtitle><description>Application of lab-scale sequencing batch (SBR) and sequencing batch biofilm reactors (SBBR) for treatment of dairy wastewater was investigated under organic loading of 1,130-1,560 gBOD 5 /m 3 ·d. The main characteristics of the dairy wastewater were: pH=4.9, chemical oxygen demand (COD)=16,264 mg/ l ; biological oxygen demand (BOD 5 )=10,536 mg/ l , PO 4 -P=342 mg/ l ; total nitrogen (TN)=224 mg/ l . SBBR was filled with the Kaldnes K1 biocarrier at 30% of the volume of empty reactor. The SBR and SBBR were operated in fixed 24 h cycles, each consisting of 30 min fill up, 22 h aeration, 1.5 h settle, 30 min decant, and idle with a hydraulic retention time (HRT) of 8 days. Operational parameters such as pH, dissolved oxygen (DO), mixed liquor suspended solid (MLSS), solids retention time (SRT) and sludge volume index (SVI) were monitored during the whole cycle. The effects of these parameters on the COD, nitrogen and phosphorus removal were discussed in this paper. As a result, adding biocarrier to the reactor had a positive effect on organic with COD removal of 63.5% for SBR and 81.8% for SBBR and nutrient removal with ammonium removal of 66.0% for SBR and 85.1% for SBBR in treatment of dairy wastewater.</description><subject>Aeration</subject><subject>Biofilms</subject><subject>Biotechnology</subject><subject>Catalysis</subject><subject>Chemical oxygen demand</subject><subject>Chemistry</subject><subject>Chemistry and Materials Science</subject><subject>Decantation</subject><subject>Environmental Engineering</subject><subject>Hydraulic retention time</subject><subject>Industrial Chemistry/Chemical Engineering</subject><subject>Materials Science</subject><subject>Organic chemistry</subject><subject>Parameters</subject><subject>Phosphorus removal</subject><subject>Sludge</subject><subject>Solid suspensions</subject><subject>Wastewater treatment</subject><subject>화학공학</subject><issn>0256-1115</issn><issn>1975-7220</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2019</creationdate><recordtype>article</recordtype><recordid>eNp1kEtLAzEUhYMoWKs_wF3AjV2M3mQmnWTZFh-FglDrOmQymZo-JjVJKf33po7gysXlLO53DvcehG4JPBCA8jEQwkmRAeFpBM_oGeoRUbKspBTOUQ8oG2aEEHaJrkJYATA2pNBDi9Fut7FaReta7BoczNfetNq2S1ypqD9xZV1jN1vsjdLReXz_Ph7PB9i2uFbWH_FBhWgOKhqPY2Li1rTxGl00ahPMza_20cfz02Lyms3eXqaT0SzTOYOYGcV5DorlRuWsoIxrKIhgNRWapF1TgYCypk2tS8WoNgVXggx1XkBV1oLyvI8GXW7rG7nWVjplf3Tp5NrL0XwxlQUIAeLE3nXszrv0Yohy5fa-TedJSsqc58OClYkiHaW9C8GbRu683Sp_lATkqWjZFS1T0fJUtKTJQztPSGy7NP4v-X_TN3YwfxI</recordid><startdate>20190201</startdate><enddate>20190201</enddate><creator>Ozturk, Arzu</creator><creator>Aygun, Ahmet</creator><creator>Nas, Bilgehan</creator><general>Springer US</general><general>Springer Nature B.V</general><general>한국화학공학회</general><scope>AAYXX</scope><scope>CITATION</scope><scope>ACYCR</scope></search><sort><creationdate>20190201</creationdate><title>Application of sequencing batch biofilm reactor (SBBR) in dairy wastewater treatment</title><author>Ozturk, Arzu ; Aygun, Ahmet ; Nas, Bilgehan</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c350t-ea8830a53ea354258c04195d29c1ea8fb0907d2fdc7a52ce48a916c340b7d9283</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2019</creationdate><topic>Aeration</topic><topic>Biofilms</topic><topic>Biotechnology</topic><topic>Catalysis</topic><topic>Chemical oxygen demand</topic><topic>Chemistry</topic><topic>Chemistry and Materials Science</topic><topic>Decantation</topic><topic>Environmental Engineering</topic><topic>Hydraulic retention time</topic><topic>Industrial Chemistry/Chemical Engineering</topic><topic>Materials Science</topic><topic>Organic chemistry</topic><topic>Parameters</topic><topic>Phosphorus removal</topic><topic>Sludge</topic><topic>Solid suspensions</topic><topic>Wastewater treatment</topic><topic>화학공학</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Ozturk, Arzu</creatorcontrib><creatorcontrib>Aygun, Ahmet</creatorcontrib><creatorcontrib>Nas, Bilgehan</creatorcontrib><collection>CrossRef</collection><collection>Korean Citation Index</collection><jtitle>The Korean journal of chemical engineering</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Ozturk, Arzu</au><au>Aygun, Ahmet</au><au>Nas, Bilgehan</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Application of sequencing batch biofilm reactor (SBBR) in dairy wastewater treatment</atitle><jtitle>The Korean journal of chemical engineering</jtitle><stitle>Korean J. Chem. Eng</stitle><date>2019-02-01</date><risdate>2019</risdate><volume>36</volume><issue>2</issue><spage>248</spage><epage>254</epage><pages>248-254</pages><issn>0256-1115</issn><eissn>1975-7220</eissn><abstract>Application of lab-scale sequencing batch (SBR) and sequencing batch biofilm reactors (SBBR) for treatment of dairy wastewater was investigated under organic loading of 1,130-1,560 gBOD 5 /m 3 ·d. The main characteristics of the dairy wastewater were: pH=4.9, chemical oxygen demand (COD)=16,264 mg/ l ; biological oxygen demand (BOD 5 )=10,536 mg/ l , PO 4 -P=342 mg/ l ; total nitrogen (TN)=224 mg/ l . SBBR was filled with the Kaldnes K1 biocarrier at 30% of the volume of empty reactor. The SBR and SBBR were operated in fixed 24 h cycles, each consisting of 30 min fill up, 22 h aeration, 1.5 h settle, 30 min decant, and idle with a hydraulic retention time (HRT) of 8 days. Operational parameters such as pH, dissolved oxygen (DO), mixed liquor suspended solid (MLSS), solids retention time (SRT) and sludge volume index (SVI) were monitored during the whole cycle. The effects of these parameters on the COD, nitrogen and phosphorus removal were discussed in this paper. As a result, adding biocarrier to the reactor had a positive effect on organic with COD removal of 63.5% for SBR and 81.8% for SBBR and nutrient removal with ammonium removal of 66.0% for SBR and 85.1% for SBBR in treatment of dairy wastewater.</abstract><cop>New York</cop><pub>Springer US</pub><doi>10.1007/s11814-018-0198-2</doi><tpages>7</tpages></addata></record>
fulltext fulltext
identifier ISSN: 0256-1115
ispartof Korean Journal of Chemical Engineering, 2019, 36(2), 227, pp.248-254
issn 0256-1115
1975-7220
language eng
recordid cdi_nrf_kci_oai_kci_go_kr_ARTI_4099098
source Springer Nature
subjects Aeration
Biofilms
Biotechnology
Catalysis
Chemical oxygen demand
Chemistry
Chemistry and Materials Science
Decantation
Environmental Engineering
Hydraulic retention time
Industrial Chemistry/Chemical Engineering
Materials Science
Organic chemistry
Parameters
Phosphorus removal
Sludge
Solid suspensions
Wastewater treatment
화학공학
title Application of sequencing batch biofilm reactor (SBBR) in dairy wastewater treatment
url http://sfxeu10.hosted.exlibrisgroup.com/loughborough?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2024-12-28T11%3A05%3A19IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-proquest_nrf_k&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=Application%20of%20sequencing%20batch%20biofilm%20reactor%20(SBBR)%20in%20dairy%20wastewater%20treatment&rft.jtitle=The%20Korean%20journal%20of%20chemical%20engineering&rft.au=Ozturk,%20Arzu&rft.date=2019-02-01&rft.volume=36&rft.issue=2&rft.spage=248&rft.epage=254&rft.pages=248-254&rft.issn=0256-1115&rft.eissn=1975-7220&rft_id=info:doi/10.1007/s11814-018-0198-2&rft_dat=%3Cproquest_nrf_k%3E2173836457%3C/proquest_nrf_k%3E%3Cgrp_id%3Ecdi_FETCH-LOGICAL-c350t-ea8830a53ea354258c04195d29c1ea8fb0907d2fdc7a52ce48a916c340b7d9283%3C/grp_id%3E%3Coa%3E%3C/oa%3E%3Curl%3E%3C/url%3E&rft_id=info:oai/&rft_pqid=2173836457&rft_id=info:pmid/&rfr_iscdi=true