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<dublin_core schema="dc">
<dcvalue element="contributor" qualifier="author">Park,&#x20;Chanhyuk</dcvalue>
<dcvalue element="contributor" qualifier="author">Lee,&#x20;Young&#x20;Haeng</dcvalue>
<dcvalue element="contributor" qualifier="author">Lee,&#x20;Sanghyup</dcvalue>
<dcvalue element="contributor" qualifier="author">Hong,&#x20;Seungkwan</dcvalue>
<dcvalue element="date" qualifier="accessioned">2024-01-20T23:33:48Z</dcvalue>
<dcvalue element="date" qualifier="available">2024-01-20T23:33:48Z</dcvalue>
<dcvalue element="date" qualifier="created">2021-09-03</dcvalue>
<dcvalue element="date" qualifier="issued">2008-03-01</dcvalue>
<dcvalue element="identifier" qualifier="issn">0011-9164</dcvalue>
<dcvalue element="identifier" qualifier="uri">https:&#x2F;&#x2F;pubs.kist.re.kr&#x2F;handle&#x2F;201004&#x2F;133661</dcvalue>
<dcvalue element="description" qualifier="abstract">A&#x20;series&#x20;of&#x20;reverse&#x20;osmosis&#x20;(RO)&#x20;membrane&#x20;filtration&#x20;experiments&#x20;was&#x20;performed&#x20;systematically&#x20;in&#x20;order&#x20;to&#x20;investigate&#x20;the&#x20;effects&#x20;of&#x20;various&#x20;hydrodynamic&#x20;and&#x20;physicochemical&#x20;operational&#x20;parameters&#x20;on&#x20;a&#x20;cake&#x20;layer&#x20;formation&#x20;in&#x20;colloidal&#x20;and&#x20;particulate&#x20;suspensions.&#x20;Bench-scale&#x20;fouling&#x20;experiments&#x20;with&#x20;a&#x20;thin-film&#x20;composite&#x20;RO&#x20;membrane&#x20;were&#x20;performed&#x20;at&#x20;various&#x20;combinations&#x20;of&#x20;trans-membrane&#x20;pressure&#x20;(TMP),&#x20;cross-flow&#x20;velocity&#x20;(CFV),&#x20;particle&#x20;size,&#x20;pH,&#x20;and&#x20;ionic&#x20;strength.&#x20;In&#x20;this&#x20;study,&#x20;silica&#x20;particles&#x20;with&#x20;two&#x20;different&#x20;mean&#x20;diameters&#x20;of&#x20;0.1&#x20;and&#x20;3.0&#x20;mu&#x20;m&#x20;were&#x20;used&#x20;as&#x20;model&#x20;colloids.&#x20;Membrane&#x20;filtration&#x20;experiments&#x20;with&#x20;colloidal&#x20;suspensions&#x20;under&#x20;various&#x20;hydrodynamic&#x20;operating&#x20;conditions&#x20;resulted&#x20;that&#x20;more&#x20;significant&#x20;permeate&#x20;flux&#x20;decline&#x20;was&#x20;observed&#x20;as&#x20;TMP&#x20;increased&#x20;and&#x20;CFV&#x20;decreased,&#x20;which&#x20;was&#x20;attributed&#x20;to&#x20;the&#x20;higher&#x20;accumulative&#x20;mass&#x20;of&#x20;particles&#x20;on&#x20;the&#x20;membrane&#x20;surface.&#x20;Results&#x20;of&#x20;fouling&#x20;experiments&#x20;under&#x20;various&#x20;physicochemical&#x20;operating&#x20;conditions&#x20;demonstrated&#x20;that&#x20;the&#x20;rate&#x20;of&#x20;flux&#x20;decline&#x20;decreased&#x20;significantly&#x20;with&#x20;an&#x20;increase&#x20;of&#x20;the&#x20;ionic&#x20;strength&#x20;as&#x20;well&#x20;as&#x20;particle&#x20;size,&#x20;while&#x20;the&#x20;flux&#x20;decline&#x20;rate&#x20;did&#x20;not&#x20;vary&#x20;when&#x20;solution&#x20;pH&#x20;changed.&#x20;The&#x20;experimentally&#x20;measured&#x20;cake&#x20;layer&#x20;thickness&#x20;increased&#x20;with&#x20;a&#x20;decrease&#x20;in&#x20;particle&#x20;size&#x20;and&#x20;solution&#x20;ionic&#x20;strength.&#x20;Furthermore,&#x20;the&#x20;model&#x20;estimation&#x20;of&#x20;cake&#x20;layer&#x20;thickness&#x20;by&#x20;using&#x20;a&#x20;cake&#x20;filtration&#x20;theory&#x20;based&#x20;on&#x20;the&#x20;hydraulic&#x20;resistance&#x20;of&#x20;membrane&#x20;and&#x20;cake&#x20;layer&#x20;was&#x20;performed&#x20;under&#x20;various&#x20;ionic&#x20;strength&#x20;conditions.&#x20;The&#x20;primary&#x20;model&#x20;parameters&#x20;including&#x20;accumulated&#x20;mass&#x20;and&#x20;specific&#x20;cake&#x20;resistance&#x20;were&#x20;calculated&#x20;from&#x20;the&#x20;cake&#x20;layer&#x20;resistance.&#x20;This&#x20;result&#x20;indicated&#x20;that&#x20;the&#x20;formation&#x20;of&#x20;cake&#x20;layer&#x20;could&#x20;be&#x20;closely&#x20;related&#x20;with&#x20;solution&#x20;water&#x20;chemistry.&#x20;The&#x20;model&#x20;estimated&#x20;cake&#x20;layer&#x20;thickness&#x20;values&#x20;were&#x20;in&#x20;good&#x20;agreement&#x20;with&#x20;the&#x20;experimentally&#x20;measured&#x20;values.</dcvalue>
<dcvalue element="language" qualifier="none">English</dcvalue>
<dcvalue element="publisher" qualifier="none">ELSEVIER&#x20;SCIENCE&#x20;BV</dcvalue>
<dcvalue element="subject" qualifier="none">MONTE-CARLO-SIMULATION</dcvalue>
<dcvalue element="subject" qualifier="none">PERMEATE&#x20;FLUX&#x20;DECLINE</dcvalue>
<dcvalue element="subject" qualifier="none">CROSS-FLOW&#x20;FILTRATION</dcvalue>
<dcvalue element="subject" qualifier="none">CONCENTRATION&#x20;POLARIZATION</dcvalue>
<dcvalue element="subject" qualifier="none">MODEL&#x20;DEVELOPMENT</dcvalue>
<dcvalue element="subject" qualifier="none">PORE&#x20;BLOCKAGE</dcvalue>
<dcvalue element="subject" qualifier="none">MICROFILTRATION</dcvalue>
<dcvalue element="subject" qualifier="none">DIFFUSION</dcvalue>
<dcvalue element="subject" qualifier="none">ULTRAFILTRATION</dcvalue>
<dcvalue element="subject" qualifier="none">PERFORMANCE</dcvalue>
<dcvalue element="title" qualifier="none">Effect&#x20;of&#x20;cake&#x20;layer&#x20;structure&#x20;on&#x20;colloidal&#x20;fouling&#x20;in&#x20;reverse&#x20;osmosis&#x20;membranes</dcvalue>
<dcvalue element="type" qualifier="none">Article</dcvalue>
<dcvalue element="identifier" qualifier="doi">10.1016&#x2F;j.desal.2007.01.038</dcvalue>
<dcvalue element="description" qualifier="journalClass">1</dcvalue>
<dcvalue element="identifier" qualifier="bibliographicCitation">DESALINATION,&#x20;v.220,&#x20;no.1-3,&#x20;pp.335&#x20;-&#x20;344</dcvalue>
<dcvalue element="citation" qualifier="title">DESALINATION</dcvalue>
<dcvalue element="citation" qualifier="volume">220</dcvalue>
<dcvalue element="citation" qualifier="number">1-3</dcvalue>
<dcvalue element="citation" qualifier="startPage">335</dcvalue>
<dcvalue element="citation" qualifier="endPage">344</dcvalue>
<dcvalue element="description" qualifier="journalRegisteredClass">scie</dcvalue>
<dcvalue element="description" qualifier="journalRegisteredClass">scopus</dcvalue>
<dcvalue element="identifier" qualifier="wosid">000254024800032</dcvalue>
<dcvalue element="identifier" qualifier="scopusid">2-s2.0-38349016917</dcvalue>
<dcvalue element="relation" qualifier="journalWebOfScienceCategory">Engineering,&#x20;Chemical</dcvalue>
<dcvalue element="relation" qualifier="journalWebOfScienceCategory">Water&#x20;Resources</dcvalue>
<dcvalue element="relation" qualifier="journalResearchArea">Engineering</dcvalue>
<dcvalue element="relation" qualifier="journalResearchArea">Water&#x20;Resources</dcvalue>
<dcvalue element="type" qualifier="docType">Article;&#x20;Proceedings&#x20;Paper</dcvalue>
<dcvalue element="subject" qualifier="keywordPlus">MONTE-CARLO-SIMULATION</dcvalue>
<dcvalue element="subject" qualifier="keywordPlus">PERMEATE&#x20;FLUX&#x20;DECLINE</dcvalue>
<dcvalue element="subject" qualifier="keywordPlus">CROSS-FLOW&#x20;FILTRATION</dcvalue>
<dcvalue element="subject" qualifier="keywordPlus">CONCENTRATION&#x20;POLARIZATION</dcvalue>
<dcvalue element="subject" qualifier="keywordPlus">MODEL&#x20;DEVELOPMENT</dcvalue>
<dcvalue element="subject" qualifier="keywordPlus">PORE&#x20;BLOCKAGE</dcvalue>
<dcvalue element="subject" qualifier="keywordPlus">MICROFILTRATION</dcvalue>
<dcvalue element="subject" qualifier="keywordPlus">DIFFUSION</dcvalue>
<dcvalue element="subject" qualifier="keywordPlus">ULTRAFILTRATION</dcvalue>
<dcvalue element="subject" qualifier="keywordPlus">PERFORMANCE</dcvalue>
<dcvalue element="subject" qualifier="keywordAuthor">cake&#x20;layer&#x20;thickness</dcvalue>
<dcvalue element="subject" qualifier="keywordAuthor">colloidal&#x20;fouling</dcvalue>
<dcvalue element="subject" qualifier="keywordAuthor">cake&#x20;filtration&#x20;theory</dcvalue>
<dcvalue element="subject" qualifier="keywordAuthor">reverse&#x20;osmosis</dcvalue>
</dublin_core>
