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<dc:title>Pore size analysis from retention of neutral solutes through nanofiltration membranes. The contribution of concentration–polarization</dc:title>
<dc:creator>García Martín, Noemí</dc:creator>
<dc:creator>Silva, Verónica</dc:creator>
<dc:creator>Carmona Del Rio, Francisco Javier</dc:creator>
<dc:creator>Palacio Martínez, Laura</dc:creator>
<dc:creator>Hernández Giménez, Antonio</dc:creator>
<dc:creator>Prádanos del Pico, Pedro Lourdes</dc:creator>
<dc:subject>Nanofiltration</dc:subject>
<dc:subject>Mass transfer</dc:subject>
<dc:subject>Retention</dc:subject>
<dc:subject>Pore size distribution</dc:subject>
<dc:description>Producción Científica</dc:description>
<dc:description>Pore size distribution is one of the most important characteristics of a membrane. This can be obtained from the&#xd;
fitting of pore radius calculated fromretention versus flux measurements for a set of solute solutions. In thiswork&#xd;
a set of non-charged similar molecules is chosen as solutes to minimize other interactions apart of those related&#xd;
to size. The hydrodynamic model will be used to characterize the behavior of the membrane to uncharged&#xd;
solutes, assuming that membrane pores are straight and cylindrical.&#xd;
As is known, the phenomenon of concentration polarization must be taken into account because true retention is&#xd;
not experimentally accessible by concentration measurements. Frequently, the film layer model is applied for the&#xd;
dependence of concentration with experimental conditions; but the application of this model requires prior&#xd;
knowledge of the mass transfer coefficientwhich is evaluated by different dimensionless correlations (Sherwood&#xd;
correlation). Here we show a review of different alternatives in doing it and analyze their consequences when&#xd;
computing the pore size distribution.&#xd;
Experimental data were obtained from dead-end filtration experiments of a set of four ethylene glycol solutions&#xd;
with a nanofiltration membrane. Obtained results show the importance of the mass transfer model in the pore&#xd;
size value obtained.</dc:description>
<dc:date>2016-12-22T08:54:50Z</dc:date>
<dc:date>2016-12-22T08:54:50Z</dc:date>
<dc:date>2014</dc:date>
<dc:type>info:eu-repo/semantics/article</dc:type>
<dc:identifier>Desalination 2014, vol. 344, p. 1–11</dc:identifier>
<dc:identifier>0011-9164</dc:identifier>
<dc:identifier>http://uvadoc.uva.es/handle/10324/21899</dc:identifier>
<dc:identifier>10.1016/j.desal.2014.02.038</dc:identifier>
<dc:language>eng</dc:language>
<dc:relation>http://www.sciencedirect.com/science/article/pii/S001191641400112X</dc:relation>
<dc:rights>info:eu-repo/semantics/openAccess</dc:rights>
<dc:rights>http://creativecommons.org/licenses/by-nc-nd/4.0/</dc:rights>
<dc:rights>Attribution-NonCommercial-NoDerivatives 4.0 International</dc:rights>
<dc:publisher>Elsevier</dc:publisher>
<dc:peerreviewed>SI</dc:peerreviewed>
</ow:Publication>
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