2026-04-28T08:15:11Zhttps://riubu.ubu.es/oai/requestoai:riubu.ubu.es:10259/45682022-04-29T12:02:46Zcom_10259_4244com_10259_5086com_10259_2604col_10259_4245
Roque Viadas, Lara
2d8283d9-974e-4c7e-b850-23659b742050
500
Escudero Barbero, Isabel
161
500
Benito Moreno, José Manuel
58
500
2017-08-24T10:37:29Z
2019-06-08T02:45:07Z
2017-06
1383-5866
http://hdl.handle.net/10259/4568
10.1016/j.seppur.2017.02.048
The ultrafiltration process for separation of sodium lactate from sorbitan monooleate (Span 80) and
sodium dodecyl sulfate (SDS) surfactants using ZrO2 flat-disc ultrafiltration membranes was studied in
this work. The study is focused on the influence of the nominal molecular weight limit of the membrane
(NMWL), the transmembrane pressure (TMP), and initial lactic acid concentration (CA) on the permeate
flux (Jp) and rejections observed to ion lactate (RA) and SDS (RS) using a full central composite experimental
design and response surface methodology.
Experiments were conducted in four stages: a first stage of lactic acid extraction with niosomes formulated
with Span 80 (20 mol/m3) and SDS (4 mol/m3), a second back-extraction stage conducted by NaOH
addition until pH > 12 for niosomes breaking and sodium lactate releasing, and a third and fourth ultrafiltration
stages at 25 C to separate the lactate ions from the mixed surfactants.
Membrane NMWL, TMP and their interactions presented statistically significant influence on the permeate
flux. Rejections to lactate ion and SDS were lower than 4.5% and higher than 86%, respectively,
whereas Span 80 rejection was 100% in all range of experimental conditions tested.
The optimal conditions were established for maximum values of permeate flux, and they were obtained
for a 2 bar TMP and 15 kDa NMWL membrane. Under these conditions, the rejections of SDS surfactant
and lactate ion were 87.3% and 4.31%, respectively, with a permeate flux of 42.63 L/m2 h. The antagonistic
effect between permeate flux and SDS rejection is also proved.
Ministerio de Economía y Competitividad
(MINECO, Spain) through project CTQ2011-25239, and from Junta de Castilla y León through project BU055U16 cofinanced by the European Regional Development Fund (ERDFFEDER) is gratefully acknowledged
application/pdf
eng
Elsevier
Separation and Purification Technology. 2017, V. 180, p. 90-98
https://doi.org/10.1016/j.seppur.2017.02.048
Attribution-NonCommercial-NoDerivatives 4.0 International
http://creativecommons.org/licenses/by-nc-nd/4.0/
info:eu-repo/semantics/openAccess
Lactic acid
Span 80
SDS
Ultrafiltration
Experimental design methodology
Chemical engineering
Ingeniería química
Separation of sodium lactate from Span 80 and SDS surfactants by ultrafiltration
info:eu-repo/semantics/article
info:eu-repo/semantics/acceptedVersion
CC-LICENSE
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Roque-SPT_2017.pdf.txt
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10259/4568
oai:riubu.ubu.es:10259/4568
2022-04-29 14:02:46.921
Repositorio Institucional de la Universidad de Burgos
bubrep@ubu.es
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