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<rdf:RDF xmlns:rdf="http://www.w3.org/1999/02/22-rdf-syntax-ns#" xmlns:dc="http://purl.org/dc/elements/1.1/"><rdf:Description rdf:about="https://dk.um.si/IzpisGradiva.php?id=27461"><dc:title>The removal of reactive dye printing compounds using nanofiltration</dc:title><dc:creator>Petrinić,	Irena	(Avtor)
	</dc:creator><dc:creator>Raj Andersen,	Niels Peder	(Avtor)
	</dc:creator><dc:creator>Šostar-Turk,	Sonja	(Avtor)
	</dc:creator><dc:creator>Majcen Le Marechal,	Alenka	(Avtor)
	</dc:creator><dc:subject>nanofiltration</dc:subject><dc:subject>nanofitration membranes</dc:subject><dc:subject>wastewater after reactive printing</dc:subject><dc:subject>reactive dye</dc:subject><dc:subject>concentration polarization</dc:subject><dc:description>A synthetically prepared reactive dye print wastewater, mimicking real wastewater obtained from a local textile mill, was treated by nanofiltration using an NFT-50 membrane in a plate and frame module configuration at different cross-flow velocities (0.4, 0.6 and 0.8 m/s) and pressures (2-15 bar). The nanofiltration membrane was evaluated for membrane fouling, permeate flux and its suitability for removing colour, conductivity, Na+ ions and COD as a function of operating pressure and feed concentration. The permeate separation efficiency was monitored by measuring the removal efficiency of colour, conductivity, Na+ ions and COD retention. The membrane achieved high dye retention for each of the four dyes (from 99.4 to 99.9%) and electrolytes used (63-73%). The retention of organic substances varied between 20 and 50%, depending on the pressure used; higher retentions were achieved at higher pressure and by using higher cross-flow velocities.</dc:description><dc:date>2007</dc:date><dc:date>2012-06-01 11:17:35</dc:date><dc:type>Neznano</dc:type><dc:identifier>27461</dc:identifier><dc:language>sl</dc:language></rdf:Description></rdf:RDF>
