Relative shear deformation of non-newtonian liquids in impeller induced flow

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dc.contributor.authorWichterle, Kamil
dc.contributor.authorMitschka, Pavel
dc.date.accessioned2007-08-29T08:28:27Z
dc.date.available2007-08-29T08:28:27Z
dc.date.issued1998
dc.description.abstract-enFlow induced by rotating bodies is studied from the viewpoint of the shear of liquid particles. By solution of the boundary layer equations for Newtonian and power-law non-Newtonian liquids at a rotating disc, a typical velocity field was obtained. The shear distribution of particles leaving the disc edge shows that the most important deformation occurs in the boundary layer. Distribution of shear from the viewpoint of the volume flow rate is also presented. Application of the results to the prediction of particle-breakup dynamics at rotating impellers is discussed.en
dc.identifier.citationCollection of Czechoslovak Chemical Communications. 1998, vol. 63, issue 12, p. 2092-2102.en
dc.identifier.doi10.1135/cccc19982092
dc.identifier.issn0010-0765
dc.identifier.issn1212-6950
dc.identifier.locationVe fondu ÚKen
dc.identifier.urihttp://hdl.handle.net/10084/62316
dc.identifier.wos000077887300014
dc.language.isoenen
dc.publisherAkademie věd České republiky, Ústav organické chemie a biochemieen
dc.relation.ispartofseriesCollection of Czechoslovak Chemical Communicationsen
dc.relation.urihttps://doi.org/10.1135/cccc19982092en
dc.subjectboundary layeren
dc.subjectrotating discen
dc.subjectshearen
dc.subjectparticle breakupen
dc.subjectnon-Newtonian liquidsen
dc.titleRelative shear deformation of non-newtonian liquids in impeller induced flowen
dc.typearticleen

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