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...

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Veröffentlicht in:Journal of chemical technology and biotechnology (1986) 2005-11, Vol.80 (11), p.1261-1267
Hauptverfasser: Sánchez, Omar, Aspé, Estrella, Martí, María C, Roeckel, Marlene
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container_end_page 1267
container_issue 11
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container_title Journal of chemical technology and biotechnology (1986)
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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
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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 &amp; 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. 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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. 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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 &amp; 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. 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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
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