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<mods:namePart>Roque Viadas, Lara</mods:namePart>
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<mods:namePart>Escudero Barbero, Isabel</mods:namePart>
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<mods:namePart>Benito Moreno, José Manuel</mods:namePart>
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<mods:dateAccessioned encoding="iso8601">2017-08-24T10:37:29Z</mods:dateAccessioned>
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<mods:dateIssued encoding="iso8601">2017-06</mods:dateIssued>
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<mods:identifier type="issn">1383-5866</mods:identifier>
<mods:identifier type="uri">http://hdl.handle.net/10259/4568</mods:identifier>
<mods:identifier type="doi">10.1016/j.seppur.2017.02.048</mods:identifier>
<mods:abstract>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.</mods:abstract>
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<mods:accessCondition type="useAndReproduction">Attribution-NonCommercial-NoDerivatives 4.0 International</mods:accessCondition>
<mods:subject>
<mods:topic>Lactic acid</mods:topic>
</mods:subject>
<mods:subject>
<mods:topic>Span 80</mods:topic>
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<mods:subject>
<mods:topic>SDS</mods:topic>
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<mods:subject>
<mods:topic>Ultrafiltration</mods:topic>
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<mods:subject>
<mods:topic>Experimental design methodology</mods:topic>
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<mods:titleInfo>
<mods:title>Separation of sodium lactate from Span 80 and SDS surfactants by ultrafiltration</mods:title>
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