In ordertoincreasetheunderstandingoftheunderlyingprocessesinorganicsolventnanofiltration (OSN), astudyhasbeenundertakenaimedatclarifyingthesolvent flux behaviourofceramic nanofiltration andultrafiltration membranes.Ceramicmembraneswerechosenfortheirnon-swelling character.Purewaterandavariationof11differentorganicsolventsweremeasuredonaseriesof different ceramicmembraneswithpore-sizediametersrangingfrom0.9nmupto100nm.Toavoidany historical effects,each flux measurementwascarriedoutonanewmembrane. The flux resultswereanalysedinaphenomenologicalway,andacommonverysimplelinear relationship wasobservedbetweentheproductof flux andviscosityofthesolvent,andthetotalHansen solubility parameterofthesolvent.Thelinearrelationshipwasfoundforallmembranes,independentof the membraneporesizeandthemembranematerial.Theslopeofthelinearrelationshipwasfoundto depend exponentiallyonthepore-sizediameterandonthepolarityofthemembranesurface.Thisresult emphasizes theimportanceofviscosityinthesolventtransport,butalsoofthepolaritydifference between membranesurfaceandsolvent.Theverysimple flux modeldeduced,allowsastraightforward prediction ofthe flux ofanysolventorsolventmixture,oncethewater flux ofthemembraneisknown. At thehighpore-sizeend,thephenomenologicalmodelnaturallytransformsintotheviscous-flow or pore-flow behaviourasrequired.Atentativephysicalexplanationofthemodeltakesintoaccountthe presence andextensionofawaterlayeradsorbedtothetotalporesurfaceofthesemembranes. This workalsoshowsthatthewater flux ofahydrophilicmembranegivesagoodindicationofits molecular weightcut-off(MWCO),andthereforeofitsseparationperformanceinwater.

Unravelling the solvent flux behaviour of ceramic nanofiltration and ultrafiltration membranes

2013

Abstract

In ordertoincreasetheunderstandingoftheunderlyingprocessesinorganicsolventnanofiltration (OSN), astudyhasbeenundertakenaimedatclarifyingthesolvent flux behaviourofceramic nanofiltration andultrafiltration membranes.Ceramicmembraneswerechosenfortheirnon-swelling character.Purewaterandavariationof11differentorganicsolventsweremeasuredonaseriesof different ceramicmembraneswithpore-sizediametersrangingfrom0.9nmupto100nm.Toavoidany historical effects,each flux measurementwascarriedoutonanewmembrane. The flux resultswereanalysedinaphenomenologicalway,andacommonverysimplelinear relationship wasobservedbetweentheproductof flux andviscosityofthesolvent,andthetotalHansen solubility parameterofthesolvent.Thelinearrelationshipwasfoundforallmembranes,independentof the membraneporesizeandthemembranematerial.Theslopeofthelinearrelationshipwasfoundto depend exponentiallyonthepore-sizediameterandonthepolarityofthemembranesurface.Thisresult emphasizes theimportanceofviscosityinthesolventtransport,butalsoofthepolaritydifference between membranesurfaceandsolvent.Theverysimple flux modeldeduced,allowsastraightforward prediction ofthe flux ofanysolventorsolventmixture,oncethewater flux ofthemembraneisknown. At thehighpore-sizeend,thephenomenologicalmodelnaturallytransformsintotheviscous-flow or pore-flow behaviourasrequired.Atentativephysicalexplanationofthemodeltakesintoaccountthe presence andextensionofawaterlayeradsorbedtothetotalporesurfaceofthesemembranes. This workalsoshowsthatthewater flux ofahydrophilicmembranegivesagoodindicationofits molecular weightcut-off(MWCO),andthereforeofitsseparationperformanceinwater.
2013
Istituto per la Tecnologia delle Membrane - ITM
Nanofiltration
Modelling
Organic solvent
Ceramic membranes
Hansen parameters
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/20.500.14243/124273
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