<?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>2026-05-11T16:11:05Z</responseDate><request verb="GetRecord" identifier="oai:riubu.ubu.es:10259/4568" metadataPrefix="marc">https://riubu.ubu.es/oai/request</request><GetRecord><record><header><identifier>oai:riubu.ubu.es:10259/4568</identifier><datestamp>2022-04-29T12:02:46Z</datestamp><setSpec>com_10259_4244</setSpec><setSpec>com_10259_5086</setSpec><setSpec>com_10259_2604</setSpec><setSpec>col_10259_4245</setSpec></header><metadata><record xmlns="http://www.loc.gov/MARC21/slim" xmlns:doc="http://www.lyncode.com/xoai" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xmlns:dcterms="http://purl.org/dc/terms/" xsi:schemaLocation="http://www.loc.gov/MARC21/slim http://www.loc.gov/standards/marcxml/schema/MARC21slim.xsd">
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<datafield tag="042" ind1=" " ind2=" ">
<subfield code="a">dc</subfield>
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<datafield tag="720" ind1=" " ind2=" ">
<subfield code="a">Roque Viadas, Lara</subfield>
<subfield code="e">author</subfield>
</datafield>
<datafield tag="720" ind1=" " ind2=" ">
<subfield code="a">Escudero Barbero, Isabel</subfield>
<subfield code="e">author</subfield>
</datafield>
<datafield tag="720" ind1=" " ind2=" ">
<subfield code="a">Benito Moreno, José Manuel</subfield>
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</datafield>
<datafield tag="260" ind1=" " ind2=" ">
<subfield code="c">2017-06</subfield>
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<subfield code="a">The ultrafiltration process for separation of sodium lactate from sorbitan monooleate (Span 80) and&#xd;
sodium dodecyl sulfate (SDS) surfactants using ZrO2 flat-disc ultrafiltration membranes was studied in&#xd;
this work. The study is focused on the influence of the nominal molecular weight limit of the membrane&#xd;
(NMWL), the transmembrane pressure (TMP), and initial lactic acid concentration (CA) on the permeate&#xd;
flux (Jp) and rejections observed to ion lactate (RA) and SDS (RS) using a full central composite experimental&#xd;
design and response surface methodology.&#xd;
Experiments were conducted in four stages: a first stage of lactic acid extraction with niosomes formulated&#xd;
with Span 80 (20 mol/m3) and SDS (4 mol/m3), a second back-extraction stage conducted by NaOH&#xd;
addition until pH > 12 for niosomes breaking and sodium lactate releasing, and a third and fourth ultrafiltration&#xd;
stages at 25  C to separate the lactate ions from the mixed surfactants.&#xd;
Membrane NMWL, TMP and their interactions presented statistically significant influence on the permeate&#xd;
flux. Rejections to lactate ion and SDS were lower than 4.5% and higher than 86%, respectively,&#xd;
whereas Span 80 rejection was 100% in all range of experimental conditions tested.&#xd;
The optimal conditions were established for maximum values of permeate flux, and they were obtained&#xd;
for a 2 bar TMP and 15 kDa NMWL membrane. Under these conditions, the rejections of SDS surfactant&#xd;
and lactate ion were 87.3% and 4.31%, respectively, with a permeate flux of 42.63 L/m2 h. The antagonistic&#xd;
effect between permeate flux and SDS rejection is also proved.</subfield>
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<subfield code="a">1383-5866</subfield>
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<subfield code="a">http://hdl.handle.net/10259/4568</subfield>
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<datafield tag="024" ind2=" " ind1="8">
<subfield code="a">10.1016/j.seppur.2017.02.048</subfield>
</datafield>
<datafield ind1=" " ind2=" " tag="653">
<subfield code="a">Lactic acid</subfield>
</datafield>
<datafield ind1=" " ind2=" " tag="653">
<subfield code="a">Span 80</subfield>
</datafield>
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<subfield code="a">SDS</subfield>
</datafield>
<datafield ind1=" " ind2=" " tag="653">
<subfield code="a">Ultrafiltration</subfield>
</datafield>
<datafield ind1=" " ind2=" " tag="653">
<subfield code="a">Experimental design methodology</subfield>
</datafield>
<datafield tag="245" ind1="0" ind2="0">
<subfield code="a">Separation of sodium lactate from Span 80 and SDS surfactants by ultrafiltration</subfield>
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