Loading…

Submerged Membrane Bioreactor Configurations for Biological Nutrient Removal from Urban Wastewater: Experimental Tests and Model Simulation

Pilot-scale experimental measurements and simulations were utilised to evaluate the nutrient removal efficiency of three submerged membrane bioreactor designs. This study compared setups with post- and pre-denitrification processes. A 625 L pilot plant for treating primary effluent provided the oper...

Full description

Saved in:
Bibliographic Details
Published in:Environments (Basel, Switzerland) Switzerland), 2024-11, Vol.11 (11), p.260
Main Authors: Mouthón-Bello, Javier A., Coronado-Hernández, Oscar E., Fuertes-Miquel, Vicente S.
Format: Article
Language:English
Subjects:
Citations: Items that this one cites
Online Access:Get full text
Tags: Add Tag
No Tags, Be the first to tag this record!
cited_by
cites cdi_FETCH-LOGICAL-c197t-d503661ad9f95caaa4ce20f86cad4ad87a83df7ff0ab5aaeb6df0180d6a63cac3
container_end_page
container_issue 11
container_start_page 260
container_title Environments (Basel, Switzerland)
container_volume 11
creator Mouthón-Bello, Javier A.
Coronado-Hernández, Oscar E.
Fuertes-Miquel, Vicente S.
description Pilot-scale experimental measurements and simulations were utilised to evaluate the nutrient removal efficiency of three submerged membrane bioreactor designs. This study compared setups with post- and pre-denitrification processes. A 625 L pilot plant for treating primary effluent provided the operational data necessary for calibrating the activated sludge model, specifically for chemical oxygen demand and nitrogen removal under steady-state flow. Identical influent conditions were maintained for all configurations while varying the sludge retention times (from 5 to 100 d), hydraulic retention times (ranging from 4 to 15 h), return activated sludge flow rates (between 0.1 and 3.0), and aerobic volume fractions (from 0.3 to 1.0). The pilot plant tests showed high COD and ammonia removal (above 90%) but moderate total nitrogen removal (above 70%). The simulation results successfully forecasted the effluent concentrations of COD and nitrogen for each configuration. There were noticeable variations in the kinetic parameters, such as mass transfer coefficients and biomass decay rates, related to the activated sludge model. However, increasing the sludge retention time beyond 20 d, hydraulic retention time beyond 8 h, return activated sludge rates above 2.0, or aerobic volume fractions beyond 0.4 did not significantly enhance nutrient removal. The post-denitrification setup showed a clear benefit in nitrogen removal but required a greater oxygen supply.
doi_str_mv 10.3390/environments11110260
format article
fullrecord <record><control><sourceid>gale_proqu</sourceid><recordid>TN_cdi_proquest_journals_3133023864</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><galeid>A818199630</galeid><sourcerecordid>A818199630</sourcerecordid><originalsourceid>FETCH-LOGICAL-c197t-d503661ad9f95caaa4ce20f86cad4ad87a83df7ff0ab5aaeb6df0180d6a63cac3</originalsourceid><addsrcrecordid>eNptUcFOGzEQXVVFAlH-gIMlzqH2OvF6udGIQqW0SEDEcTVrjyOjXTsde9PyDfx0naaHHpjLjN68N29GU1Xngl9K2fLPGHaeYhgx5CRK8FrxD9VJzRs1k3WrP_5XH1dnKb1wzsVCy0bKk-rtcepHpA1a9h3HniAg--IjIZgciS1jcH4zEWQfQ2KuQKU7xI03MLAfUyZffNkDjnFXAEdxZGvqIbBnSBl_QUa6Yje_t0h-v2HhPGHKiUEohtHiwB79OA1_53-qjhwMCc_-5dNq_fXmaXk3W93fflter2ZGtE2e2QWXSgmwrWsXBgDmBmvutDJg52B1A1pa1zjHoV8AYK-s40Jzq0BJA0aeVheHuVuKP6eyTvcSJwrFspNCSl5LreaFdXlgbWDAzgcXM0GRg8XRmxjQ-YJfa6FF2yrJi2B-EBiKKRG6bluOBnrtBO_2r-ree5X8A9vJjyE</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>3133023864</pqid></control><display><type>article</type><title>Submerged Membrane Bioreactor Configurations for Biological Nutrient Removal from Urban Wastewater: Experimental Tests and Model Simulation</title><source>Publicly Available Content Database</source><creator>Mouthón-Bello, Javier A. ; Coronado-Hernández, Oscar E. ; Fuertes-Miquel, Vicente S.</creator><creatorcontrib>Mouthón-Bello, Javier A. ; Coronado-Hernández, Oscar E. ; Fuertes-Miquel, Vicente S.</creatorcontrib><description>Pilot-scale experimental measurements and simulations were utilised to evaluate the nutrient removal efficiency of three submerged membrane bioreactor designs. This study compared setups with post- and pre-denitrification processes. A 625 L pilot plant for treating primary effluent provided the operational data necessary for calibrating the activated sludge model, specifically for chemical oxygen demand and nitrogen removal under steady-state flow. Identical influent conditions were maintained for all configurations while varying the sludge retention times (from 5 to 100 d), hydraulic retention times (ranging from 4 to 15 h), return activated sludge flow rates (between 0.1 and 3.0), and aerobic volume fractions (from 0.3 to 1.0). The pilot plant tests showed high COD and ammonia removal (above 90%) but moderate total nitrogen removal (above 70%). The simulation results successfully forecasted the effluent concentrations of COD and nitrogen for each configuration. There were noticeable variations in the kinetic parameters, such as mass transfer coefficients and biomass decay rates, related to the activated sludge model. However, increasing the sludge retention time beyond 20 d, hydraulic retention time beyond 8 h, return activated sludge rates above 2.0, or aerobic volume fractions beyond 0.4 did not significantly enhance nutrient removal. The post-denitrification setup showed a clear benefit in nitrogen removal but required a greater oxygen supply.</description><identifier>ISSN: 2076-3298</identifier><identifier>EISSN: 2076-3298</identifier><identifier>DOI: 10.3390/environments11110260</identifier><language>eng</language><publisher>Basel: MDPI AG</publisher><subject>Activated sludge ; Ammonia ; Biological wastewater treatment ; Biomass ; Bioreactors ; Calibration ; Chemical oxygen demand ; Configurations ; Decay rate ; Denitrification ; Effluents ; Equilibrium flow ; Flow rates ; Hydraulic retention time ; Mass transfer ; Membranes ; Methods ; Nitrates ; Nitrogen ; Nitrogen removal ; Nutrient removal ; Pilot plants ; Purification ; Retention ; Retention time ; Sewage ; Sludge ; Software packages ; Steady state models ; Water treatment</subject><ispartof>Environments (Basel, Switzerland), 2024-11, Vol.11 (11), p.260</ispartof><rights>COPYRIGHT 2024 MDPI AG</rights><rights>2024 by the authors. Licensee MDPI, Basel, Switzerland. This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution (CC BY) license (https://creativecommons.org/licenses/by/4.0/). Notwithstanding the ProQuest Terms and Conditions, you may use this content in accordance with the terms of the License.</rights><lds50>peer_reviewed</lds50><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed><cites>FETCH-LOGICAL-c197t-d503661ad9f95caaa4ce20f86cad4ad87a83df7ff0ab5aaeb6df0180d6a63cac3</cites><orcidid>0000-0002-6574-0857 ; 0000-0003-3524-2555</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://www.proquest.com/docview/3133023864/fulltextPDF?pq-origsite=primo$$EPDF$$P50$$Gproquest$$Hfree_for_read</linktopdf><linktohtml>$$Uhttps://www.proquest.com/docview/3133023864?pq-origsite=primo$$EHTML$$P50$$Gproquest$$Hfree_for_read</linktohtml><link.rule.ids>314,780,784,25752,27923,27924,37011,44589,74997</link.rule.ids></links><search><creatorcontrib>Mouthón-Bello, Javier A.</creatorcontrib><creatorcontrib>Coronado-Hernández, Oscar E.</creatorcontrib><creatorcontrib>Fuertes-Miquel, Vicente S.</creatorcontrib><title>Submerged Membrane Bioreactor Configurations for Biological Nutrient Removal from Urban Wastewater: Experimental Tests and Model Simulation</title><title>Environments (Basel, Switzerland)</title><description>Pilot-scale experimental measurements and simulations were utilised to evaluate the nutrient removal efficiency of three submerged membrane bioreactor designs. This study compared setups with post- and pre-denitrification processes. A 625 L pilot plant for treating primary effluent provided the operational data necessary for calibrating the activated sludge model, specifically for chemical oxygen demand and nitrogen removal under steady-state flow. Identical influent conditions were maintained for all configurations while varying the sludge retention times (from 5 to 100 d), hydraulic retention times (ranging from 4 to 15 h), return activated sludge flow rates (between 0.1 and 3.0), and aerobic volume fractions (from 0.3 to 1.0). The pilot plant tests showed high COD and ammonia removal (above 90%) but moderate total nitrogen removal (above 70%). The simulation results successfully forecasted the effluent concentrations of COD and nitrogen for each configuration. There were noticeable variations in the kinetic parameters, such as mass transfer coefficients and biomass decay rates, related to the activated sludge model. However, increasing the sludge retention time beyond 20 d, hydraulic retention time beyond 8 h, return activated sludge rates above 2.0, or aerobic volume fractions beyond 0.4 did not significantly enhance nutrient removal. The post-denitrification setup showed a clear benefit in nitrogen removal but required a greater oxygen supply.</description><subject>Activated sludge</subject><subject>Ammonia</subject><subject>Biological wastewater treatment</subject><subject>Biomass</subject><subject>Bioreactors</subject><subject>Calibration</subject><subject>Chemical oxygen demand</subject><subject>Configurations</subject><subject>Decay rate</subject><subject>Denitrification</subject><subject>Effluents</subject><subject>Equilibrium flow</subject><subject>Flow rates</subject><subject>Hydraulic retention time</subject><subject>Mass transfer</subject><subject>Membranes</subject><subject>Methods</subject><subject>Nitrates</subject><subject>Nitrogen</subject><subject>Nitrogen removal</subject><subject>Nutrient removal</subject><subject>Pilot plants</subject><subject>Purification</subject><subject>Retention</subject><subject>Retention time</subject><subject>Sewage</subject><subject>Sludge</subject><subject>Software packages</subject><subject>Steady state models</subject><subject>Water treatment</subject><issn>2076-3298</issn><issn>2076-3298</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2024</creationdate><recordtype>article</recordtype><sourceid>PIMPY</sourceid><recordid>eNptUcFOGzEQXVVFAlH-gIMlzqH2OvF6udGIQqW0SEDEcTVrjyOjXTsde9PyDfx0naaHHpjLjN68N29GU1Xngl9K2fLPGHaeYhgx5CRK8FrxD9VJzRs1k3WrP_5XH1dnKb1wzsVCy0bKk-rtcepHpA1a9h3HniAg--IjIZgciS1jcH4zEWQfQ2KuQKU7xI03MLAfUyZffNkDjnFXAEdxZGvqIbBnSBl_QUa6Yje_t0h-v2HhPGHKiUEohtHiwB79OA1_53-qjhwMCc_-5dNq_fXmaXk3W93fflter2ZGtE2e2QWXSgmwrWsXBgDmBmvutDJg52B1A1pa1zjHoV8AYK-s40Jzq0BJA0aeVheHuVuKP6eyTvcSJwrFspNCSl5LreaFdXlgbWDAzgcXM0GRg8XRmxjQ-YJfa6FF2yrJi2B-EBiKKRG6bluOBnrtBO_2r-ree5X8A9vJjyE</recordid><startdate>20241101</startdate><enddate>20241101</enddate><creator>Mouthón-Bello, Javier A.</creator><creator>Coronado-Hernández, Oscar E.</creator><creator>Fuertes-Miquel, Vicente S.</creator><general>MDPI AG</general><scope>AAYXX</scope><scope>CITATION</scope><scope>ABUWG</scope><scope>AFKRA</scope><scope>ATCPS</scope><scope>AZQEC</scope><scope>BENPR</scope><scope>BHPHI</scope><scope>CCPQU</scope><scope>DWQXO</scope><scope>GNUQQ</scope><scope>HCIFZ</scope><scope>PATMY</scope><scope>PIMPY</scope><scope>PQEST</scope><scope>PQQKQ</scope><scope>PQUKI</scope><scope>PRINS</scope><scope>PYCSY</scope><orcidid>https://orcid.org/0000-0002-6574-0857</orcidid><orcidid>https://orcid.org/0000-0003-3524-2555</orcidid></search><sort><creationdate>20241101</creationdate><title>Submerged Membrane Bioreactor Configurations for Biological Nutrient Removal from Urban Wastewater: Experimental Tests and Model Simulation</title><author>Mouthón-Bello, Javier A. ; Coronado-Hernández, Oscar E. ; Fuertes-Miquel, Vicente S.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c197t-d503661ad9f95caaa4ce20f86cad4ad87a83df7ff0ab5aaeb6df0180d6a63cac3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2024</creationdate><topic>Activated sludge</topic><topic>Ammonia</topic><topic>Biological wastewater treatment</topic><topic>Biomass</topic><topic>Bioreactors</topic><topic>Calibration</topic><topic>Chemical oxygen demand</topic><topic>Configurations</topic><topic>Decay rate</topic><topic>Denitrification</topic><topic>Effluents</topic><topic>Equilibrium flow</topic><topic>Flow rates</topic><topic>Hydraulic retention time</topic><topic>Mass transfer</topic><topic>Membranes</topic><topic>Methods</topic><topic>Nitrates</topic><topic>Nitrogen</topic><topic>Nitrogen removal</topic><topic>Nutrient removal</topic><topic>Pilot plants</topic><topic>Purification</topic><topic>Retention</topic><topic>Retention time</topic><topic>Sewage</topic><topic>Sludge</topic><topic>Software packages</topic><topic>Steady state models</topic><topic>Water treatment</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Mouthón-Bello, Javier A.</creatorcontrib><creatorcontrib>Coronado-Hernández, Oscar E.</creatorcontrib><creatorcontrib>Fuertes-Miquel, Vicente S.</creatorcontrib><collection>CrossRef</collection><collection>ProQuest Central (Alumni)</collection><collection>ProQuest Central</collection><collection>Agricultural &amp; Environmental Science Collection</collection><collection>ProQuest Central Essentials</collection><collection>ProQuest Central</collection><collection>Natural Science Collection</collection><collection>ProQuest One Community College</collection><collection>ProQuest Central Korea</collection><collection>ProQuest Central Student</collection><collection>SciTech Premium Collection</collection><collection>Environmental Science Database</collection><collection>Publicly Available Content 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>ProQuest Central China</collection><collection>Environmental Science Collection</collection><jtitle>Environments (Basel, Switzerland)</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Mouthón-Bello, Javier A.</au><au>Coronado-Hernández, Oscar E.</au><au>Fuertes-Miquel, Vicente S.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Submerged Membrane Bioreactor Configurations for Biological Nutrient Removal from Urban Wastewater: Experimental Tests and Model Simulation</atitle><jtitle>Environments (Basel, Switzerland)</jtitle><date>2024-11-01</date><risdate>2024</risdate><volume>11</volume><issue>11</issue><spage>260</spage><pages>260-</pages><issn>2076-3298</issn><eissn>2076-3298</eissn><abstract>Pilot-scale experimental measurements and simulations were utilised to evaluate the nutrient removal efficiency of three submerged membrane bioreactor designs. This study compared setups with post- and pre-denitrification processes. A 625 L pilot plant for treating primary effluent provided the operational data necessary for calibrating the activated sludge model, specifically for chemical oxygen demand and nitrogen removal under steady-state flow. Identical influent conditions were maintained for all configurations while varying the sludge retention times (from 5 to 100 d), hydraulic retention times (ranging from 4 to 15 h), return activated sludge flow rates (between 0.1 and 3.0), and aerobic volume fractions (from 0.3 to 1.0). The pilot plant tests showed high COD and ammonia removal (above 90%) but moderate total nitrogen removal (above 70%). The simulation results successfully forecasted the effluent concentrations of COD and nitrogen for each configuration. There were noticeable variations in the kinetic parameters, such as mass transfer coefficients and biomass decay rates, related to the activated sludge model. However, increasing the sludge retention time beyond 20 d, hydraulic retention time beyond 8 h, return activated sludge rates above 2.0, or aerobic volume fractions beyond 0.4 did not significantly enhance nutrient removal. The post-denitrification setup showed a clear benefit in nitrogen removal but required a greater oxygen supply.</abstract><cop>Basel</cop><pub>MDPI AG</pub><doi>10.3390/environments11110260</doi><orcidid>https://orcid.org/0000-0002-6574-0857</orcidid><orcidid>https://orcid.org/0000-0003-3524-2555</orcidid><oa>free_for_read</oa></addata></record>
fulltext fulltext
identifier ISSN: 2076-3298
ispartof Environments (Basel, Switzerland), 2024-11, Vol.11 (11), p.260
issn 2076-3298
2076-3298
language eng
recordid cdi_proquest_journals_3133023864
source Publicly Available Content Database
subjects Activated sludge
Ammonia
Biological wastewater treatment
Biomass
Bioreactors
Calibration
Chemical oxygen demand
Configurations
Decay rate
Denitrification
Effluents
Equilibrium flow
Flow rates
Hydraulic retention time
Mass transfer
Membranes
Methods
Nitrates
Nitrogen
Nitrogen removal
Nutrient removal
Pilot plants
Purification
Retention
Retention time
Sewage
Sludge
Software packages
Steady state models
Water treatment
title Submerged Membrane Bioreactor Configurations for Biological Nutrient Removal from Urban Wastewater: Experimental Tests and Model Simulation
url http://sfxeu10.hosted.exlibrisgroup.com/loughborough?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-01-08T16%3A09%3A21IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-gale_proqu&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=Submerged%20Membrane%20Bioreactor%20Configurations%20for%20Biological%20Nutrient%20Removal%20from%20Urban%20Wastewater:%20Experimental%20Tests%20and%20Model%20Simulation&rft.jtitle=Environments%20(Basel,%20Switzerland)&rft.au=Mouth%C3%B3n-Bello,%20Javier%20A.&rft.date=2024-11-01&rft.volume=11&rft.issue=11&rft.spage=260&rft.pages=260-&rft.issn=2076-3298&rft.eissn=2076-3298&rft_id=info:doi/10.3390/environments11110260&rft_dat=%3Cgale_proqu%3EA818199630%3C/gale_proqu%3E%3Cgrp_id%3Ecdi_FETCH-LOGICAL-c197t-d503661ad9f95caaa4ce20f86cad4ad87a83df7ff0ab5aaeb6df0180d6a63cac3%3C/grp_id%3E%3Coa%3E%3C/oa%3E%3Curl%3E%3C/url%3E&rft_id=info:oai/&rft_pqid=3133023864&rft_id=info:pmid/&rft_galeid=A818199630&rfr_iscdi=true