Membrane pore blocking during cake formation in constant pressure and constant flux dead-end microfiltration of very dilute colloids
Dead-end microfiltration experiments of very dilute colloids of polystylene latex (PSL) were conducted under constant flux and constant pressure conditions using the track-etched polycarbonate membranes. The pressure rising behaviors in constant flux filtration were examined under different filtrati...
Gespeichert in:
Veröffentlicht in: | Chemical engineering science 2015-01, Vol.122, p.465-473 |
---|---|
Hauptverfasser: | , , , |
Format: | Artikel |
Sprache: | eng |
Schlagworte: | |
Online-Zugang: | Volltext |
Tags: |
Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
|
container_end_page | 473 |
---|---|
container_issue | |
container_start_page | 465 |
container_title | Chemical engineering science |
container_volume | 122 |
creator | Iritani, Eiji Katagiri, Nobuyuki Takenaka, Toshiharu Yamashita, Yuuki |
description | Dead-end microfiltration experiments of very dilute colloids of polystylene latex (PSL) were conducted under constant flux and constant pressure conditions using the track-etched polycarbonate membranes. The pressure rising behaviors in constant flux filtration were examined under different filtration rate and solid mass fraction conditions, and the flux decline behaviors in constant pressure filtration were examined under different pressure and solid mass fraction conditions. The combined filtration model in which the pore blocking of membrane and the cake formation on the membrane surface took place simultaneously has been developed in order to evaluate the filtration behaviors. In the model, it was assumed that all the particles rejected by the membrane contributed the cake resistance and that a part of them also served as the pore blocking resistance by reaching and completely sealing the open pores in the membrane. The intermediate blocking law was employed in the model in order to describe the pore clogging behavior of the membrane, and the model also assumed that a part of membrane pores remained open eventually. The calculations based on the model revealed the existence of the negative slope in the characteristic filtration curve based on the classical blocking filtration law, as observed in the initial period of filtration experiments. The model developed well described the pressure rising behaviors in constant flux filtration and the flux decline behaviors in constant pressure filtration.
•Pore blocking of membrane occurred during cake formation on membrane surface.•Combined filtration model describing pore blocking and cake formation was proposed.•Model calculations well evaluated negative slope in characteristic filtration curve.•The model well described pressure rising behaviors in constant flux filtration.•The model well described flux decline behaviors in constant pressure filtration. |
doi_str_mv | 10.1016/j.ces.2014.09.052 |
format | Article |
fullrecord | <record><control><sourceid>proquest_cross</sourceid><recordid>TN_cdi_proquest_miscellaneous_1669888445</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><els_id>S000925091400565X</els_id><sourcerecordid>1669888445</sourcerecordid><originalsourceid>FETCH-LOGICAL-c433t-a7a63339bf04909522c3e0b19a82a20bce7e7096ac15c884fa22c400ea8660e73</originalsourceid><addsrcrecordid>eNp9kEtLxDAUhYMoOI7-AHdZumm96Tu4ksEXjLjRdUjTW8lM2oxJOujeH26GCu5cHe7hfBfOIeSSQcqAVdebVKFPM2BFCjyFMjsiC9bUeVIUUB6TBQDwJCuBn5Iz7zfxrGsGC_L9jEPr5Ih0Zx3S1li11eM77SZ3ECW3SHvrBhm0HakeqbKjD3IMdOfQ-ykycuz-3N5Mn7RD2SUY7UErZ3ttgpt529M9ui_aaTMFjJQxVnf-nJz00ni8-NUlebu_e109JuuXh6fV7TpRRZ6HRNayyvOctz0UHHiZZSpHaBmXTSYzaBXWWAOvpGKlapqilzFRAKBsqgqwzpfkav67c_ZjQh_EoL1CY2J_O3nBqoo3ESzKGGVzNBbw3mEvdk4P0n0JBuKwuNiIuLg4LC6Ai7h4ZG5mBmOHvUYnvNI4Kuy0QxVEZ_U_9A_dIYu6</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>1669888445</pqid></control><display><type>article</type><title>Membrane pore blocking during cake formation in constant pressure and constant flux dead-end microfiltration of very dilute colloids</title><source>Elsevier ScienceDirect Journals</source><creator>Iritani, Eiji ; Katagiri, Nobuyuki ; Takenaka, Toshiharu ; Yamashita, Yuuki</creator><creatorcontrib>Iritani, Eiji ; Katagiri, Nobuyuki ; Takenaka, Toshiharu ; Yamashita, Yuuki</creatorcontrib><description>Dead-end microfiltration experiments of very dilute colloids of polystylene latex (PSL) were conducted under constant flux and constant pressure conditions using the track-etched polycarbonate membranes. The pressure rising behaviors in constant flux filtration were examined under different filtration rate and solid mass fraction conditions, and the flux decline behaviors in constant pressure filtration were examined under different pressure and solid mass fraction conditions. The combined filtration model in which the pore blocking of membrane and the cake formation on the membrane surface took place simultaneously has been developed in order to evaluate the filtration behaviors. In the model, it was assumed that all the particles rejected by the membrane contributed the cake resistance and that a part of them also served as the pore blocking resistance by reaching and completely sealing the open pores in the membrane. The intermediate blocking law was employed in the model in order to describe the pore clogging behavior of the membrane, and the model also assumed that a part of membrane pores remained open eventually. The calculations based on the model revealed the existence of the negative slope in the characteristic filtration curve based on the classical blocking filtration law, as observed in the initial period of filtration experiments. The model developed well described the pressure rising behaviors in constant flux filtration and the flux decline behaviors in constant pressure filtration.
•Pore blocking of membrane occurred during cake formation on membrane surface.•Combined filtration model describing pore blocking and cake formation was proposed.•Model calculations well evaluated negative slope in characteristic filtration curve.•The model well described pressure rising behaviors in constant flux filtration.•The model well described flux decline behaviors in constant pressure filtration.</description><identifier>ISSN: 0009-2509</identifier><identifier>EISSN: 1873-4405</identifier><identifier>DOI: 10.1016/j.ces.2014.09.052</identifier><language>eng</language><publisher>Elsevier Ltd</publisher><subject>Blocking ; Blocking filtration ; Cake filtration ; Cakes ; Constant flux filtration ; Constant pressure filtration ; Constants ; Filtration ; Flux ; Fouling ; Mathematical models ; Membranes ; Microfiltration ; Porosity</subject><ispartof>Chemical engineering science, 2015-01, Vol.122, p.465-473</ispartof><rights>2014 Elsevier Ltd</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c433t-a7a63339bf04909522c3e0b19a82a20bce7e7096ac15c884fa22c400ea8660e73</citedby><cites>FETCH-LOGICAL-c433t-a7a63339bf04909522c3e0b19a82a20bce7e7096ac15c884fa22c400ea8660e73</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://www.sciencedirect.com/science/article/pii/S000925091400565X$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,776,780,3536,27903,27904,65309</link.rule.ids></links><search><creatorcontrib>Iritani, Eiji</creatorcontrib><creatorcontrib>Katagiri, Nobuyuki</creatorcontrib><creatorcontrib>Takenaka, Toshiharu</creatorcontrib><creatorcontrib>Yamashita, Yuuki</creatorcontrib><title>Membrane pore blocking during cake formation in constant pressure and constant flux dead-end microfiltration of very dilute colloids</title><title>Chemical engineering science</title><description>Dead-end microfiltration experiments of very dilute colloids of polystylene latex (PSL) were conducted under constant flux and constant pressure conditions using the track-etched polycarbonate membranes. The pressure rising behaviors in constant flux filtration were examined under different filtration rate and solid mass fraction conditions, and the flux decline behaviors in constant pressure filtration were examined under different pressure and solid mass fraction conditions. The combined filtration model in which the pore blocking of membrane and the cake formation on the membrane surface took place simultaneously has been developed in order to evaluate the filtration behaviors. In the model, it was assumed that all the particles rejected by the membrane contributed the cake resistance and that a part of them also served as the pore blocking resistance by reaching and completely sealing the open pores in the membrane. The intermediate blocking law was employed in the model in order to describe the pore clogging behavior of the membrane, and the model also assumed that a part of membrane pores remained open eventually. The calculations based on the model revealed the existence of the negative slope in the characteristic filtration curve based on the classical blocking filtration law, as observed in the initial period of filtration experiments. The model developed well described the pressure rising behaviors in constant flux filtration and the flux decline behaviors in constant pressure filtration.
•Pore blocking of membrane occurred during cake formation on membrane surface.•Combined filtration model describing pore blocking and cake formation was proposed.•Model calculations well evaluated negative slope in characteristic filtration curve.•The model well described pressure rising behaviors in constant flux filtration.•The model well described flux decline behaviors in constant pressure filtration.</description><subject>Blocking</subject><subject>Blocking filtration</subject><subject>Cake filtration</subject><subject>Cakes</subject><subject>Constant flux filtration</subject><subject>Constant pressure filtration</subject><subject>Constants</subject><subject>Filtration</subject><subject>Flux</subject><subject>Fouling</subject><subject>Mathematical models</subject><subject>Membranes</subject><subject>Microfiltration</subject><subject>Porosity</subject><issn>0009-2509</issn><issn>1873-4405</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2015</creationdate><recordtype>article</recordtype><recordid>eNp9kEtLxDAUhYMoOI7-AHdZumm96Tu4ksEXjLjRdUjTW8lM2oxJOujeH26GCu5cHe7hfBfOIeSSQcqAVdebVKFPM2BFCjyFMjsiC9bUeVIUUB6TBQDwJCuBn5Iz7zfxrGsGC_L9jEPr5Ih0Zx3S1li11eM77SZ3ECW3SHvrBhm0HakeqbKjD3IMdOfQ-ykycuz-3N5Mn7RD2SUY7UErZ3ttgpt529M9ui_aaTMFjJQxVnf-nJz00ni8-NUlebu_e109JuuXh6fV7TpRRZ6HRNayyvOctz0UHHiZZSpHaBmXTSYzaBXWWAOvpGKlapqilzFRAKBsqgqwzpfkav67c_ZjQh_EoL1CY2J_O3nBqoo3ESzKGGVzNBbw3mEvdk4P0n0JBuKwuNiIuLg4LC6Ai7h4ZG5mBmOHvUYnvNI4Kuy0QxVEZ_U_9A_dIYu6</recordid><startdate>20150127</startdate><enddate>20150127</enddate><creator>Iritani, Eiji</creator><creator>Katagiri, Nobuyuki</creator><creator>Takenaka, Toshiharu</creator><creator>Yamashita, Yuuki</creator><general>Elsevier Ltd</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7U5</scope><scope>8FD</scope><scope>F28</scope><scope>FR3</scope><scope>L7M</scope></search><sort><creationdate>20150127</creationdate><title>Membrane pore blocking during cake formation in constant pressure and constant flux dead-end microfiltration of very dilute colloids</title><author>Iritani, Eiji ; Katagiri, Nobuyuki ; Takenaka, Toshiharu ; Yamashita, Yuuki</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c433t-a7a63339bf04909522c3e0b19a82a20bce7e7096ac15c884fa22c400ea8660e73</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2015</creationdate><topic>Blocking</topic><topic>Blocking filtration</topic><topic>Cake filtration</topic><topic>Cakes</topic><topic>Constant flux filtration</topic><topic>Constant pressure filtration</topic><topic>Constants</topic><topic>Filtration</topic><topic>Flux</topic><topic>Fouling</topic><topic>Mathematical models</topic><topic>Membranes</topic><topic>Microfiltration</topic><topic>Porosity</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Iritani, Eiji</creatorcontrib><creatorcontrib>Katagiri, Nobuyuki</creatorcontrib><creatorcontrib>Takenaka, Toshiharu</creatorcontrib><creatorcontrib>Yamashita, Yuuki</creatorcontrib><collection>CrossRef</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>Technology Research Database</collection><collection>ANTE: Abstracts in New Technology & Engineering</collection><collection>Engineering Research Database</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>Iritani, Eiji</au><au>Katagiri, Nobuyuki</au><au>Takenaka, Toshiharu</au><au>Yamashita, Yuuki</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Membrane pore blocking during cake formation in constant pressure and constant flux dead-end microfiltration of very dilute colloids</atitle><jtitle>Chemical engineering science</jtitle><date>2015-01-27</date><risdate>2015</risdate><volume>122</volume><spage>465</spage><epage>473</epage><pages>465-473</pages><issn>0009-2509</issn><eissn>1873-4405</eissn><abstract>Dead-end microfiltration experiments of very dilute colloids of polystylene latex (PSL) were conducted under constant flux and constant pressure conditions using the track-etched polycarbonate membranes. The pressure rising behaviors in constant flux filtration were examined under different filtration rate and solid mass fraction conditions, and the flux decline behaviors in constant pressure filtration were examined under different pressure and solid mass fraction conditions. The combined filtration model in which the pore blocking of membrane and the cake formation on the membrane surface took place simultaneously has been developed in order to evaluate the filtration behaviors. In the model, it was assumed that all the particles rejected by the membrane contributed the cake resistance and that a part of them also served as the pore blocking resistance by reaching and completely sealing the open pores in the membrane. The intermediate blocking law was employed in the model in order to describe the pore clogging behavior of the membrane, and the model also assumed that a part of membrane pores remained open eventually. The calculations based on the model revealed the existence of the negative slope in the characteristic filtration curve based on the classical blocking filtration law, as observed in the initial period of filtration experiments. The model developed well described the pressure rising behaviors in constant flux filtration and the flux decline behaviors in constant pressure filtration.
•Pore blocking of membrane occurred during cake formation on membrane surface.•Combined filtration model describing pore blocking and cake formation was proposed.•Model calculations well evaluated negative slope in characteristic filtration curve.•The model well described pressure rising behaviors in constant flux filtration.•The model well described flux decline behaviors in constant pressure filtration.</abstract><pub>Elsevier Ltd</pub><doi>10.1016/j.ces.2014.09.052</doi><tpages>9</tpages></addata></record> |
fulltext | fulltext |
identifier | ISSN: 0009-2509 |
ispartof | Chemical engineering science, 2015-01, Vol.122, p.465-473 |
issn | 0009-2509 1873-4405 |
language | eng |
recordid | cdi_proquest_miscellaneous_1669888445 |
source | Elsevier ScienceDirect Journals |
subjects | Blocking Blocking filtration Cake filtration Cakes Constant flux filtration Constant pressure filtration Constants Filtration Flux Fouling Mathematical models Membranes Microfiltration Porosity |
title | Membrane pore blocking during cake formation in constant pressure and constant flux dead-end microfiltration of very dilute colloids |
url | https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-01-24T03%3A50%3A52IST&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=Membrane%20pore%20blocking%20during%20cake%20formation%20in%20constant%20pressure%20and%20constant%20flux%20dead-end%20microfiltration%20of%20very%20dilute%20colloids&rft.jtitle=Chemical%20engineering%20science&rft.au=Iritani,%20Eiji&rft.date=2015-01-27&rft.volume=122&rft.spage=465&rft.epage=473&rft.pages=465-473&rft.issn=0009-2509&rft.eissn=1873-4405&rft_id=info:doi/10.1016/j.ces.2014.09.052&rft_dat=%3Cproquest_cross%3E1669888445%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=1669888445&rft_id=info:pmid/&rft_els_id=S000925091400565X&rfr_iscdi=true |