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Studies on modelling and simulation of lactose hydrolysis by free and immobilized β-galactosidase from Aspergillus niger

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dc.contributor.author Papayannakos, N en
dc.contributor.author Markas, G en
dc.contributor.author Kekos, D en
dc.date.accessioned 2014-03-01T01:41:56Z
dc.date.available 2014-03-01T01:41:56Z
dc.date.issued 1993 en
dc.identifier.issn 03009467 en
dc.identifier.uri https://dspace.lib.ntua.gr/xmlui/handle/123456789/23673
dc.relation.uri http://www.scopus.com/inward/record.url?eid=2-s2.0-0027639561&partnerID=40&md5=03af3dfc8ca21d443c1c37f738d5cc12 en
dc.subject.other Hydrolysis en
dc.subject.other PH en
dc.subject.other Pollution control en
dc.subject.other Waste utilization en
dc.subject.other Cottage cheese en
dc.subject.other Dairy industry en
dc.subject.other Immobilization en
dc.subject.other Organic carriers en
dc.subject.other Sweetening valve en
dc.subject.other Enzyme kinetics en
dc.title Studies on modelling and simulation of lactose hydrolysis by free and immobilized β-galactosidase from Aspergillus niger en
heal.type journalArticle en
heal.publicationDate 1993 en
heal.abstract β-Galactosidase from Aspergillus niger was immobilized effectively on a porous ceramic monolith by adsorption and intermolecular cross-linking. The binding efficiency reached 80% and no enzyme leaching was observed even under vigorous mechanical agitation. Immobilization did not change the pH optimum of lactose hydrolysis. The enzyme decay followed first-order kinetics and the thermal stability of the immobilized lactase was considerably enhanced. At 50 °C and pH 3.6 the half-life of the immobilized lactase was 180 days and that of the free enzyme 24 days. The kinetics of lactose hydrolysis by both free and immobilized lactase were studied in a batch reactor system in the absence of any mass transfer limitations. In both cases the totally competitive galactose inhibition kinetic model predicted the experimental data. Simulation of the performance of a laboratory continuous flow immobilized lactase reactor system showed that experimental results could be predicted by the ideal plug flow model when an apparent effectiveness factor nf=0.65 is used to take into account the external mass transfer limitations. © 1993. en
heal.journalName The Chemical Engineering Journal en
dc.identifier.volume 52 en
dc.identifier.issue 1 en
dc.identifier.spage B1 en
dc.identifier.epage B12 en


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