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Modification of the kinetics for modeling substrate storage and biomass growth mechanism in activated sludge system under aerobic condition
Based on the activated sludge model no.3 (ASM3), a new kinetic expression describing substrate removal and biomass growth mechanism occurring in activated sludge system under aerobic condition was established. The new model proposed that under feast condition, one part of substrate was utilized dire...
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Published in: | Chemical engineering science 2012-08, Vol.78, p.75-81 |
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creator | Fan, Ji Vanrolleghem, Peter A. Lu, Shuguang Qiu, Zhaofu |
description | Based on the activated sludge model no.3 (ASM3), a new kinetic expression describing substrate removal and biomass growth mechanism occurring in activated sludge system under aerobic condition was established. The new model proposed that under feast condition, one part of substrate was utilized directly for biomass growth and the other part was stored as internal storage products and simultaneously the storage products were used for biomass growth. The model was successfully calibrated on oxygen uptake rate (OUR) data and off-line soluble chemical oxygen demand (COD) dynamic variations obtained from batch experiments with biomass from a full-scale wastewater treatment plant (WWTP). OUR predictions with the calibrated model could reasonably describe the OUR profile after pulse addition of acetate, i.e., the OUR transiently reached a very high level, and then increased gradually to a maximum level until the initial substrate was taken up for storage and biomass growth. This new model also, for the first time, highlighted the significant effect of the biomass storage products concentration before pulse addition of acetate on OUR profile.
► During feast phase the SSSG process includes storage and growth using XSTO or substrate processes. ► There is no Monod inhibition function for the consumption of XSTO. ► The XSTO concentration before pulse addition of acetate can affect OUR profile. |
doi_str_mv | 10.1016/j.ces.2012.05.004 |
format | article |
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► During feast phase the SSSG process includes storage and growth using XSTO or substrate processes. ► There is no Monod inhibition function for the consumption of XSTO. ► The XSTO concentration before pulse addition of acetate can affect OUR profile.</description><identifier>ISSN: 0009-2509</identifier><identifier>EISSN: 1873-4405</identifier><identifier>DOI: 10.1016/j.ces.2012.05.004</identifier><identifier>CODEN: CESCAC</identifier><language>eng</language><publisher>Kidlington: Elsevier Ltd</publisher><subject>Acetates ; Activated sludge ; Aircraft components ; Applied sciences ; Biomass ; Calibration ; Chemical engineering ; chemical oxygen demand ; Exact sciences and technology ; General purification processes ; Kinetics ; Mathematical modeling ; Mathematical models ; oxygen ; Oxygen demand ; Oxygen uptake rate (OUR) ; Parameter identification ; Pollution ; prediction ; Sewerage works: sewers, sewage treatment plants, outfalls ; Simulation ; Simultaneous substrate storage and growth (SSSG) ; wastewater treatment ; Wastewaters ; Water treatment and pollution</subject><ispartof>Chemical engineering science, 2012-08, Vol.78, p.75-81</ispartof><rights>2012 Elsevier Ltd</rights><rights>2015 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c417t-1484da97bc404b28ea7a327d5bdcbf9006deef9661d26e563658b09fc71b07573</citedby><cites>FETCH-LOGICAL-c417t-1484da97bc404b28ea7a327d5bdcbf9006deef9661d26e563658b09fc71b07573</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,780,784,27924,27925</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=26340503$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Fan, Ji</creatorcontrib><creatorcontrib>Vanrolleghem, Peter A.</creatorcontrib><creatorcontrib>Lu, Shuguang</creatorcontrib><creatorcontrib>Qiu, Zhaofu</creatorcontrib><title>Modification of the kinetics for modeling substrate storage and biomass growth mechanism in activated sludge system under aerobic condition</title><title>Chemical engineering science</title><description>Based on the activated sludge model no.3 (ASM3), a new kinetic expression describing substrate removal and biomass growth mechanism occurring in activated sludge system under aerobic condition was established. The new model proposed that under feast condition, one part of substrate was utilized directly for biomass growth and the other part was stored as internal storage products and simultaneously the storage products were used for biomass growth. The model was successfully calibrated on oxygen uptake rate (OUR) data and off-line soluble chemical oxygen demand (COD) dynamic variations obtained from batch experiments with biomass from a full-scale wastewater treatment plant (WWTP). OUR predictions with the calibrated model could reasonably describe the OUR profile after pulse addition of acetate, i.e., the OUR transiently reached a very high level, and then increased gradually to a maximum level until the initial substrate was taken up for storage and biomass growth. This new model also, for the first time, highlighted the significant effect of the biomass storage products concentration before pulse addition of acetate on OUR profile.
► During feast phase the SSSG process includes storage and growth using XSTO or substrate processes. ► There is no Monod inhibition function for the consumption of XSTO. ► The XSTO concentration before pulse addition of acetate can affect OUR profile.</description><subject>Acetates</subject><subject>Activated sludge</subject><subject>Aircraft components</subject><subject>Applied sciences</subject><subject>Biomass</subject><subject>Calibration</subject><subject>Chemical engineering</subject><subject>chemical oxygen demand</subject><subject>Exact sciences and technology</subject><subject>General purification processes</subject><subject>Kinetics</subject><subject>Mathematical modeling</subject><subject>Mathematical models</subject><subject>oxygen</subject><subject>Oxygen demand</subject><subject>Oxygen uptake rate (OUR)</subject><subject>Parameter identification</subject><subject>Pollution</subject><subject>prediction</subject><subject>Sewerage works: sewers, sewage treatment plants, outfalls</subject><subject>Simulation</subject><subject>Simultaneous substrate storage and growth (SSSG)</subject><subject>wastewater treatment</subject><subject>Wastewaters</subject><subject>Water treatment and pollution</subject><issn>0009-2509</issn><issn>1873-4405</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2012</creationdate><recordtype>article</recordtype><recordid>eNqFkU2LFDEQhhtRcFz9AZ7MRfDSbaU76Q88ybJ-wIoH3XNIJ5WZjN3Jmkqv7G_wT5thFo96CgXP-1aop6pecmg48P7tsTFITQu8bUA2AOJRtePj0NVCgHxc7QBgqlsJ09PqGdGxjMPAYVf9_hKtd97o7GNg0bF8QPbDB8zeEHMxsTVaXHzYM9pmyklnZJRj0ntkOlg2-7hqIrZP8Vc-sBXNQQdPK_OBaZP9XQlYRstmS4DuKePKtmAxMY0pzt4wE4P1p_XPqydOL4QvHt6L6ubD1ffLT_X114-fL99f10bwIddcjMLqaZiNADG3I-pBd-1g5WzN7CaA3iK6qe-5bXuUfdfLcYbJmYHPMMihu6jenHtvU_y5IWW1ejK4LDpg3EjxXnIhBJ_k_1EJshPdKKGg_IyaFIkSOnWb_KrTveKgTo7UURVH6uRIgVTFUcm8fqjXZPTikg7G099g23fFHnSFe3XmnI5K71Nhbr6VIlk8tlM3joV4dyawHO7OY1JkPAaD1ic0Wdno__GPPzHfskI</recordid><startdate>20120820</startdate><enddate>20120820</enddate><creator>Fan, Ji</creator><creator>Vanrolleghem, Peter A.</creator><creator>Lu, Shuguang</creator><creator>Qiu, Zhaofu</creator><general>Elsevier Ltd</general><general>Elsevier</general><scope>FBQ</scope><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7QH</scope><scope>7QO</scope><scope>7ST</scope><scope>7UA</scope><scope>8FD</scope><scope>C1K</scope><scope>F1W</scope><scope>FR3</scope><scope>H97</scope><scope>L.G</scope><scope>P64</scope><scope>SOI</scope><scope>7SU</scope><scope>7TB</scope><scope>7U5</scope><scope>F28</scope><scope>KR7</scope><scope>L7M</scope></search><sort><creationdate>20120820</creationdate><title>Modification of the kinetics for modeling substrate storage and biomass growth mechanism in activated sludge system under aerobic condition</title><author>Fan, Ji ; Vanrolleghem, Peter A. ; Lu, Shuguang ; Qiu, Zhaofu</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c417t-1484da97bc404b28ea7a327d5bdcbf9006deef9661d26e563658b09fc71b07573</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2012</creationdate><topic>Acetates</topic><topic>Activated sludge</topic><topic>Aircraft components</topic><topic>Applied sciences</topic><topic>Biomass</topic><topic>Calibration</topic><topic>Chemical engineering</topic><topic>chemical oxygen demand</topic><topic>Exact sciences and technology</topic><topic>General purification processes</topic><topic>Kinetics</topic><topic>Mathematical modeling</topic><topic>Mathematical models</topic><topic>oxygen</topic><topic>Oxygen demand</topic><topic>Oxygen uptake rate (OUR)</topic><topic>Parameter identification</topic><topic>Pollution</topic><topic>prediction</topic><topic>Sewerage works: sewers, sewage treatment plants, outfalls</topic><topic>Simulation</topic><topic>Simultaneous substrate storage and growth (SSSG)</topic><topic>wastewater treatment</topic><topic>Wastewaters</topic><topic>Water treatment and pollution</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Fan, Ji</creatorcontrib><creatorcontrib>Vanrolleghem, Peter A.</creatorcontrib><creatorcontrib>Lu, Shuguang</creatorcontrib><creatorcontrib>Qiu, Zhaofu</creatorcontrib><collection>AGRIS</collection><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Aqualine</collection><collection>Biotechnology Research Abstracts</collection><collection>Environment 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) 3: Aquatic Pollution & Environmental Quality</collection><collection>Aquatic Science & Fisheries Abstracts (ASFA) Professional</collection><collection>Biotechnology and BioEngineering Abstracts</collection><collection>Environment Abstracts</collection><collection>Environmental Engineering Abstracts</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>ANTE: Abstracts in New Technology & Engineering</collection><collection>Civil Engineering Abstracts</collection><collection>Advanced Technologies Database with Aerospace</collection><jtitle>Chemical engineering science</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Fan, Ji</au><au>Vanrolleghem, Peter A.</au><au>Lu, Shuguang</au><au>Qiu, Zhaofu</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Modification of the kinetics for modeling substrate storage and biomass growth mechanism in activated sludge system under aerobic condition</atitle><jtitle>Chemical engineering science</jtitle><date>2012-08-20</date><risdate>2012</risdate><volume>78</volume><spage>75</spage><epage>81</epage><pages>75-81</pages><issn>0009-2509</issn><eissn>1873-4405</eissn><coden>CESCAC</coden><abstract>Based on the activated sludge model no.3 (ASM3), a new kinetic expression describing substrate removal and biomass growth mechanism occurring in activated sludge system under aerobic condition was established. The new model proposed that under feast condition, one part of substrate was utilized directly for biomass growth and the other part was stored as internal storage products and simultaneously the storage products were used for biomass growth. The model was successfully calibrated on oxygen uptake rate (OUR) data and off-line soluble chemical oxygen demand (COD) dynamic variations obtained from batch experiments with biomass from a full-scale wastewater treatment plant (WWTP). OUR predictions with the calibrated model could reasonably describe the OUR profile after pulse addition of acetate, i.e., the OUR transiently reached a very high level, and then increased gradually to a maximum level until the initial substrate was taken up for storage and biomass growth. This new model also, for the first time, highlighted the significant effect of the biomass storage products concentration before pulse addition of acetate on OUR profile.
► During feast phase the SSSG process includes storage and growth using XSTO or substrate processes. ► There is no Monod inhibition function for the consumption of XSTO. ► The XSTO concentration before pulse addition of acetate can affect OUR profile.</abstract><cop>Kidlington</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.ces.2012.05.004</doi><tpages>7</tpages></addata></record> |
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subjects | Acetates Activated sludge Aircraft components Applied sciences Biomass Calibration Chemical engineering chemical oxygen demand Exact sciences and technology General purification processes Kinetics Mathematical modeling Mathematical models oxygen Oxygen demand Oxygen uptake rate (OUR) Parameter identification Pollution prediction Sewerage works: sewers, sewage treatment plants, outfalls Simulation Simultaneous substrate storage and growth (SSSG) wastewater treatment Wastewaters Water treatment and pollution |
title | Modification of the kinetics for modeling substrate storage and biomass growth mechanism in activated sludge system under aerobic condition |
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