Rate of ammonia oxidation in a synthetic saline wastewater by a nitrifying mixed-culture
Most of the kinetic studies on nitrification have been performed in diluted salts medium. In this work, the ammonia oxidation rate (AOR) was determined by respirometry at different ammonia (0.01 and 33.5 mg N‐NH3 L−1), nitrite (0–450 mg N‐NO2− L−1) and nitrate (0 and 275 mg N‐NO3− L−1) concentration...
Gespeichert in:
Veröffentlicht in: | Journal of chemical technology and biotechnology (1986) 2005-11, Vol.80 (11), p.1261-1267 |
---|---|
Hauptverfasser: | , , , |
Format: | Artikel |
Sprache: | eng |
Schlagworte: | |
Online-Zugang: | Volltext |
Tags: |
Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
|
container_end_page | 1267 |
---|---|
container_issue | 11 |
container_start_page | 1261 |
container_title | Journal of chemical technology and biotechnology (1986) |
container_volume | 80 |
creator | Sánchez, Omar Aspé, Estrella Martí, María C Roeckel, Marlene |
description | Most of the kinetic studies on nitrification have been performed in diluted salts medium. In this work, the ammonia oxidation rate (AOR) was determined by respirometry at different ammonia (0.01 and 33.5 mg N‐NH3 L−1), nitrite (0–450 mg N‐NO2− L−1) and nitrate (0 and 275 mg N‐NO3− L−1) concentrations in a saline medium at 30 °C and pH 7.5. Sodium azide was used to uncouple the ammonia and nitrite oxidation, so as to measure independently the AOR. It was determined that ammonia causes substrate inhibition and that nitrite and nitrate exhibit product inhibition upon the AOR. The effects of ammonia, nitrite and nitrate were represented by the Andrews equation (maximal ammonia oxidation rate, rAOMAX, = 43.2 [mg N‐NH3 (g VSSAO h)−1]; half saturation constant, KSAO, = 0.11 mg N‐NH3 L−1; inhibition constant KIAO, = 7.65 mg N‐NH3 L−1), by the non‐competitive inhibition model (inhibition constant, KINI, = 176 mg N‐NO2− L−1) and by the partially competitive inhibition model (inhibition constant, KINA, = 3.3 mg N‐NO3− L−1; α factor = 0.24), respectively. The rAOMAX value is smaller, and the KSAO value larger, than the values reported in diluted salts medium; the KIAO value is comparable to those reported. Process simulations with the kinetic model in batch nitrifying reactors showed that the inhibitory effects of nitrite and nitrate are significant for initial ammonia concentrations larger than 100 mg N‐NH4+ L−1. Copyright © 2005 Society of Chemical Industry |
doi_str_mv | 10.1002/jctb.1320 |
format | Article |
fullrecord | <record><control><sourceid>proquest_cross</sourceid><recordid>TN_cdi_proquest_miscellaneous_29028842</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>29028842</sourcerecordid><originalsourceid>FETCH-LOGICAL-c4340-a5357c74408ee7c697685a05e5ddee56661afc50ec94088ff78e5a4e702309f63</originalsourceid><addsrcrecordid>eNp1kM1u1DAURi0EEkNhwRt4AxKLtDdO_JMlDLRQtaVCRWVn3XquwSVxiu3RTN6ejGZUVqy-zfnO4jD2uobjGkCc3Ltyd1w3Ap6wRQ2drlql4ClbgFCmElLL5-xFzvcAoIxQC_bjGxbio-c4DGMMyMdtWGEJY-QhcuR5iuUXleB4xj5E4hvMhTbzKfG7aQZiKCn4KcSffAhbWlVu3Zd1opfsmcc-06vDHrHvp59ulp-ri69nX5bvLyrXNi1UKBupnW5bMETaqU4rIxEkydWKSCqlavROArluRoz32pDEljSIBjqvmiP2du99SOOfNeVih5Ad9T1GGtfZig6EMa2YwXd70KUx50TePqQwYJpsDXbXzu7a2V27mX1zkGJ22PuE0YX876DrToDecSd7bhN6mv4vtOfLmw8Hc7V_hDnj9vGB6bdVutHS3l6d2cvr6_bjLZxa0_wFRXGNLA</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>29028842</pqid></control><display><type>article</type><title>Rate of ammonia oxidation in a synthetic saline wastewater by a nitrifying mixed-culture</title><source>Wiley Online Library Journals Frontfile Complete</source><creator>Sánchez, Omar ; Aspé, Estrella ; Martí, María C ; Roeckel, Marlene</creator><creatorcontrib>Sánchez, Omar ; Aspé, Estrella ; Martí, María C ; Roeckel, Marlene</creatorcontrib><description>Most of the kinetic studies on nitrification have been performed in diluted salts medium. In this work, the ammonia oxidation rate (AOR) was determined by respirometry at different ammonia (0.01 and 33.5 mg N‐NH3 L−1), nitrite (0–450 mg N‐NO2− L−1) and nitrate (0 and 275 mg N‐NO3− L−1) concentrations in a saline medium at 30 °C and pH 7.5. Sodium azide was used to uncouple the ammonia and nitrite oxidation, so as to measure independently the AOR. It was determined that ammonia causes substrate inhibition and that nitrite and nitrate exhibit product inhibition upon the AOR. The effects of ammonia, nitrite and nitrate were represented by the Andrews equation (maximal ammonia oxidation rate, rAOMAX, = 43.2 [mg N‐NH3 (g VSSAO h)−1]; half saturation constant, KSAO, = 0.11 mg N‐NH3 L−1; inhibition constant KIAO, = 7.65 mg N‐NH3 L−1), by the non‐competitive inhibition model (inhibition constant, KINI, = 176 mg N‐NO2− L−1) and by the partially competitive inhibition model (inhibition constant, KINA, = 3.3 mg N‐NO3− L−1; α factor = 0.24), respectively. The rAOMAX value is smaller, and the KSAO value larger, than the values reported in diluted salts medium; the KIAO value is comparable to those reported. Process simulations with the kinetic model in batch nitrifying reactors showed that the inhibitory effects of nitrite and nitrate are significant for initial ammonia concentrations larger than 100 mg N‐NH4+ L−1. Copyright © 2005 Society of Chemical Industry</description><identifier>ISSN: 0268-2575</identifier><identifier>EISSN: 1097-4660</identifier><identifier>DOI: 10.1002/jctb.1320</identifier><identifier>CODEN: JCTBDC</identifier><language>eng</language><publisher>Chichester, UK: John Wiley & Sons, Ltd</publisher><subject>Applied sciences ; Biological and medical sciences ; Biological treatment of waters ; Biotechnology ; Environment and pollution ; Exact sciences and technology ; Fundamental and applied biological sciences. Psychology ; General purification processes ; Industrial applications and implications. Economical aspects ; inhibition kinetic ; modeling ; nitrification ; Pollution ; saline wastewater ; Wastewaters ; Water treatment and pollution</subject><ispartof>Journal of chemical technology and biotechnology (1986), 2005-11, Vol.80 (11), p.1261-1267</ispartof><rights>Copyright © 2005 Society of Chemical Industry</rights><rights>2006 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c4340-a5357c74408ee7c697685a05e5ddee56661afc50ec94088ff78e5a4e702309f63</citedby><cites>FETCH-LOGICAL-c4340-a5357c74408ee7c697685a05e5ddee56661afc50ec94088ff78e5a4e702309f63</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%2Fjctb.1320$$EPDF$$P50$$Gwiley$$H</linktopdf><linktohtml>$$Uhttps://onlinelibrary.wiley.com/doi/full/10.1002%2Fjctb.1320$$EHTML$$P50$$Gwiley$$H</linktohtml><link.rule.ids>314,777,781,1412,27905,27906,45555,45556</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=17192070$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Sánchez, Omar</creatorcontrib><creatorcontrib>Aspé, Estrella</creatorcontrib><creatorcontrib>Martí, María C</creatorcontrib><creatorcontrib>Roeckel, Marlene</creatorcontrib><title>Rate of ammonia oxidation in a synthetic saline wastewater by a nitrifying mixed-culture</title><title>Journal of chemical technology and biotechnology (1986)</title><addtitle>J. Chem. Technol. Biotechnol</addtitle><description>Most of the kinetic studies on nitrification have been performed in diluted salts medium. In this work, the ammonia oxidation rate (AOR) was determined by respirometry at different ammonia (0.01 and 33.5 mg N‐NH3 L−1), nitrite (0–450 mg N‐NO2− L−1) and nitrate (0 and 275 mg N‐NO3− L−1) concentrations in a saline medium at 30 °C and pH 7.5. Sodium azide was used to uncouple the ammonia and nitrite oxidation, so as to measure independently the AOR. It was determined that ammonia causes substrate inhibition and that nitrite and nitrate exhibit product inhibition upon the AOR. The effects of ammonia, nitrite and nitrate were represented by the Andrews equation (maximal ammonia oxidation rate, rAOMAX, = 43.2 [mg N‐NH3 (g VSSAO h)−1]; half saturation constant, KSAO, = 0.11 mg N‐NH3 L−1; inhibition constant KIAO, = 7.65 mg N‐NH3 L−1), by the non‐competitive inhibition model (inhibition constant, KINI, = 176 mg N‐NO2− L−1) and by the partially competitive inhibition model (inhibition constant, KINA, = 3.3 mg N‐NO3− L−1; α factor = 0.24), respectively. The rAOMAX value is smaller, and the KSAO value larger, than the values reported in diluted salts medium; the KIAO value is comparable to those reported. Process simulations with the kinetic model in batch nitrifying reactors showed that the inhibitory effects of nitrite and nitrate are significant for initial ammonia concentrations larger than 100 mg N‐NH4+ L−1. Copyright © 2005 Society of Chemical Industry</description><subject>Applied sciences</subject><subject>Biological and medical sciences</subject><subject>Biological treatment of waters</subject><subject>Biotechnology</subject><subject>Environment and pollution</subject><subject>Exact sciences and technology</subject><subject>Fundamental and applied biological sciences. Psychology</subject><subject>General purification processes</subject><subject>Industrial applications and implications. Economical aspects</subject><subject>inhibition kinetic</subject><subject>modeling</subject><subject>nitrification</subject><subject>Pollution</subject><subject>saline wastewater</subject><subject>Wastewaters</subject><subject>Water treatment and pollution</subject><issn>0268-2575</issn><issn>1097-4660</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2005</creationdate><recordtype>article</recordtype><recordid>eNp1kM1u1DAURi0EEkNhwRt4AxKLtDdO_JMlDLRQtaVCRWVn3XquwSVxiu3RTN6ejGZUVqy-zfnO4jD2uobjGkCc3Ltyd1w3Ap6wRQ2drlql4ClbgFCmElLL5-xFzvcAoIxQC_bjGxbio-c4DGMMyMdtWGEJY-QhcuR5iuUXleB4xj5E4hvMhTbzKfG7aQZiKCn4KcSffAhbWlVu3Zd1opfsmcc-06vDHrHvp59ulp-ri69nX5bvLyrXNi1UKBupnW5bMETaqU4rIxEkydWKSCqlavROArluRoz32pDEljSIBjqvmiP2du99SOOfNeVih5Ad9T1GGtfZig6EMa2YwXd70KUx50TePqQwYJpsDXbXzu7a2V27mX1zkGJ22PuE0YX876DrToDecSd7bhN6mv4vtOfLmw8Hc7V_hDnj9vGB6bdVutHS3l6d2cvr6_bjLZxa0_wFRXGNLA</recordid><startdate>200511</startdate><enddate>200511</enddate><creator>Sánchez, Omar</creator><creator>Aspé, Estrella</creator><creator>Martí, María C</creator><creator>Roeckel, Marlene</creator><general>John Wiley & Sons, Ltd</general><general>Wiley</general><scope>BSCLL</scope><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>8FD</scope><scope>F28</scope><scope>FR3</scope><scope>KR7</scope></search><sort><creationdate>200511</creationdate><title>Rate of ammonia oxidation in a synthetic saline wastewater by a nitrifying mixed-culture</title><author>Sánchez, Omar ; Aspé, Estrella ; Martí, María C ; Roeckel, Marlene</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c4340-a5357c74408ee7c697685a05e5ddee56661afc50ec94088ff78e5a4e702309f63</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2005</creationdate><topic>Applied sciences</topic><topic>Biological and medical sciences</topic><topic>Biological treatment of waters</topic><topic>Biotechnology</topic><topic>Environment and pollution</topic><topic>Exact sciences and technology</topic><topic>Fundamental and applied biological sciences. Psychology</topic><topic>General purification processes</topic><topic>Industrial applications and implications. Economical aspects</topic><topic>inhibition kinetic</topic><topic>modeling</topic><topic>nitrification</topic><topic>Pollution</topic><topic>saline wastewater</topic><topic>Wastewaters</topic><topic>Water treatment and pollution</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Sánchez, Omar</creatorcontrib><creatorcontrib>Aspé, Estrella</creatorcontrib><creatorcontrib>Martí, María C</creatorcontrib><creatorcontrib>Roeckel, Marlene</creatorcontrib><collection>Istex</collection><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Technology Research Database</collection><collection>ANTE: Abstracts in New Technology & Engineering</collection><collection>Engineering Research Database</collection><collection>Civil Engineering Abstracts</collection><jtitle>Journal of chemical technology and biotechnology (1986)</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Sánchez, Omar</au><au>Aspé, Estrella</au><au>Martí, María C</au><au>Roeckel, Marlene</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Rate of ammonia oxidation in a synthetic saline wastewater by a nitrifying mixed-culture</atitle><jtitle>Journal of chemical technology and biotechnology (1986)</jtitle><addtitle>J. Chem. Technol. Biotechnol</addtitle><date>2005-11</date><risdate>2005</risdate><volume>80</volume><issue>11</issue><spage>1261</spage><epage>1267</epage><pages>1261-1267</pages><issn>0268-2575</issn><eissn>1097-4660</eissn><coden>JCTBDC</coden><abstract>Most of the kinetic studies on nitrification have been performed in diluted salts medium. In this work, the ammonia oxidation rate (AOR) was determined by respirometry at different ammonia (0.01 and 33.5 mg N‐NH3 L−1), nitrite (0–450 mg N‐NO2− L−1) and nitrate (0 and 275 mg N‐NO3− L−1) concentrations in a saline medium at 30 °C and pH 7.5. Sodium azide was used to uncouple the ammonia and nitrite oxidation, so as to measure independently the AOR. It was determined that ammonia causes substrate inhibition and that nitrite and nitrate exhibit product inhibition upon the AOR. The effects of ammonia, nitrite and nitrate were represented by the Andrews equation (maximal ammonia oxidation rate, rAOMAX, = 43.2 [mg N‐NH3 (g VSSAO h)−1]; half saturation constant, KSAO, = 0.11 mg N‐NH3 L−1; inhibition constant KIAO, = 7.65 mg N‐NH3 L−1), by the non‐competitive inhibition model (inhibition constant, KINI, = 176 mg N‐NO2− L−1) and by the partially competitive inhibition model (inhibition constant, KINA, = 3.3 mg N‐NO3− L−1; α factor = 0.24), respectively. The rAOMAX value is smaller, and the KSAO value larger, than the values reported in diluted salts medium; the KIAO value is comparable to those reported. Process simulations with the kinetic model in batch nitrifying reactors showed that the inhibitory effects of nitrite and nitrate are significant for initial ammonia concentrations larger than 100 mg N‐NH4+ L−1. Copyright © 2005 Society of Chemical Industry</abstract><cop>Chichester, UK</cop><pub>John Wiley & Sons, Ltd</pub><doi>10.1002/jctb.1320</doi><tpages>7</tpages></addata></record> |
fulltext | fulltext |
identifier | ISSN: 0268-2575 |
ispartof | Journal of chemical technology and biotechnology (1986), 2005-11, Vol.80 (11), p.1261-1267 |
issn | 0268-2575 1097-4660 |
language | eng |
recordid | cdi_proquest_miscellaneous_29028842 |
source | Wiley Online Library Journals Frontfile Complete |
subjects | Applied sciences Biological and medical sciences Biological treatment of waters Biotechnology Environment and pollution Exact sciences and technology Fundamental and applied biological sciences. Psychology General purification processes Industrial applications and implications. Economical aspects inhibition kinetic modeling nitrification Pollution saline wastewater Wastewaters Water treatment and pollution |
title | Rate of ammonia oxidation in a synthetic saline wastewater by a nitrifying mixed-culture |
url | https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-01-17T21%3A51%3A23IST&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=Rate%20of%20ammonia%20oxidation%20in%20a%20synthetic%20saline%20wastewater%20by%20a%20nitrifying%20mixed-culture&rft.jtitle=Journal%20of%20chemical%20technology%20and%20biotechnology%20(1986)&rft.au=S%C3%A1nchez,%20Omar&rft.date=2005-11&rft.volume=80&rft.issue=11&rft.spage=1261&rft.epage=1267&rft.pages=1261-1267&rft.issn=0268-2575&rft.eissn=1097-4660&rft.coden=JCTBDC&rft_id=info:doi/10.1002/jctb.1320&rft_dat=%3Cproquest_cross%3E29028842%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=29028842&rft_id=info:pmid/&rfr_iscdi=true |