<?xml version="1.0" encoding="UTF-8"?><?xml-stylesheet type="text/xsl" href="static/style.xsl"?><OAI-PMH xmlns="http://www.openarchives.org/OAI/2.0/" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xsi:schemaLocation="http://www.openarchives.org/OAI/2.0/ http://www.openarchives.org/OAI/2.0/OAI-PMH.xsd"><responseDate>2026-05-30T19:32:10Z</responseDate><request verb="GetRecord" identifier="oai:riuma.uma.es:10630/35167" metadataPrefix="marc">https://riuma.uma.es/rest/oai/request</request><GetRecord><record><header><identifier>oai:riuma.uma.es:10630/35167</identifier><datestamp>2026-02-03T10:58:58Z</datestamp><setSpec>com_10630_2254</setSpec><setSpec>col_10630_37953</setSpec></header><metadata><record xmlns="http://www.loc.gov/MARC21/slim" xmlns:dcterms="http://purl.org/dc/terms/" xmlns:doc="http://www.lyncode.com/xoai" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xsi:schemaLocation="http://www.loc.gov/MARC21/slim http://www.loc.gov/standards/marcxml/schema/MARC21slim.xsd">
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   <datafield ind2=" " ind1=" " tag="720">
      <subfield code="a">Rizki, Zulhaj</subfield>
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   <datafield ind2=" " ind1=" " tag="720">
      <subfield code="a">Janssen, Anja E.M.</subfield>
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      <subfield code="a">Hendrix, Eligius María Theodorus</subfield>
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      <subfield code="a">van der Padt, Albert</subfield>
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      <subfield code="a">Boom, Remko M.</subfield>
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      <subfield code="a">Claassen, G.D.H.</subfield>
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      <subfield code="c">2020</subfield>
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      <subfield code="a">Inhomogeneous membrane cascade systems have been utilized to purify fructooligosaccharides (FOS).&#xd;
Such a process allows a different setup at every stage of the cascade. Varying the setup at every stage implies an optimization problem related to the selection of the membrane and combinations of operating conditions. This paper solves the optimization problem for an inhomogeneous 3-stage membrane cas- cade and uses the solution as a design guideline. The optimization problem in the 3-stage membrane cas- cade design has been formulated as a mixed integer, non-linear programming model and solved using the global optimization solver, BARON. By maximizing the yield repetitively with varying purity require- ments, a frontier curve has been constructed. The frontier curve was mapped showing the window of operation. The map guides towards the setup that promotes higher permeation in the feed stage when we switch from high yield to high purity. On the other hand, the setup selection at the bottom stage does not show a clear switch, which indicates that the selection at this stage is less critical.</subfield>
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      <subfield code="a">Rizki, Z.,  Janssen, A.E.M.,  Hendrix, E.M.T.,  van  der  Padt, A., Boom, R.M. and Claassen, G.D.H. (2021), Design optimization of a 3-stage membrane cascade for oligosaccharides purification using mixed integer non-linear programming, Chemical  Engineering  Science,  231, 116275</subfield>
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      <subfield code="a">https://hdl.handle.net/10630/35167</subfield>
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      <subfield code="a">10.1016/j.ces.2020.116275</subfield>
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      <subfield code="a">Programación no lineal</subfield>
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      <subfield code="a">Design optimization of a 3-stage membrane cascade for oligosaccharides purification using mixed integer non-linear programming.</subfield>
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