<?xml version="1.0"?>
<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=27093"><dc:title>Enzymatic reactions in high-pressure membrane reactors</dc:title><dc:creator>Leitgeb,	Maja	(Avtor)
	</dc:creator><dc:creator>Primožič,	Mateja	(Avtor)
	</dc:creator><dc:creator>Knez,	Željko	(Avtor)
	</dc:creator><dc:subject>chemical processing</dc:subject><dc:subject>high pressure technology</dc:subject><dc:subject>membrane reactors</dc:subject><dc:subject>biotechnology</dc:subject><dc:description>In the studies on the stability of biocatalysts in a high-pressure batch stirred tank reactor, changes in biocatalyst activity due to pressurizationždepressurization steps were observed. An interesting alternative to overcome this inconvenience is using the high-pressure continuous membrane reactors, where just a single compression and expansion step is necessary. The aim of the research was to carry out the enzyme-catalyzed reactions in high-pressure membrane reactors. At first, high-pressure enzyme-catalyzed hydrolyses of oleyl oleate and sunflower oil were performed in a high-pressure continuous enzymatic flat-shape membrane reactor. Additionally, cellulase from Humicola insolens was covalently immobilized on tubular membrane, and enzyme-catalyzed hydrolysis of carboxy-methyl cellulose was carried out in a high-pressure continuous enzymatic tubular membrane reactor. The membrane-stability tests for flat-shape polysulfon membranes before and after treatment with supercritical CO2 or subcritical propane were done, as well.</dc:description><dc:date>2005</dc:date><dc:date>2012-06-01 09:47:49</dc:date><dc:type>Neznano</dc:type><dc:identifier>27093</dc:identifier><dc:language>sl</dc:language></rdf:Description></rdf:RDF>
