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A single segment differential tube model with interchain tube pressure effect

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dc.contributor.author Dhole, S en
dc.contributor.author Leygue, A en
dc.contributor.author Bailly, C en
dc.contributor.author Keunings, R en
dc.date.accessioned 2014-03-01T01:29:38Z
dc.date.available 2014-03-01T01:29:38Z
dc.date.issued 2009 en
dc.identifier.issn 0377-0257 en
dc.identifier.uri https://dspace.lib.ntua.gr/xmlui/handle/123456789/19333
dc.subject Convective constraint release en
dc.subject Finite extensibility en
dc.subject Interchain tube pressure effect en
dc.subject Tube model en
dc.subject.classification Mechanics en
dc.subject.other Convective constraint release en
dc.subject.other Entangled polymers en
dc.subject.other Entangled system en
dc.subject.other Experimental errors en
dc.subject.other Extensional flows en
dc.subject.other Finite extensibility en
dc.subject.other Interchain tube pressure effect en
dc.subject.other Linear polymers en
dc.subject.other Monodisperse en
dc.subject.other Nonlinear behaviours en
dc.subject.other Quantitative prediction en
dc.subject.other Relative importance en
dc.subject.other Relaxation mechanism en
dc.subject.other Reptation en
dc.subject.other Single segments en
dc.subject.other Tube dimension en
dc.subject.other Tube length en
dc.subject.other Tube model en
dc.subject.other Supramolecular chemistry en
dc.subject.other Tubes (components) en
dc.subject.other Pressure effects en
dc.title A single segment differential tube model with interchain tube pressure effect en
heal.type journalArticle en
heal.identifier.primary 10.1016/j.jnnfm.2009.03.014 en
heal.identifier.secondary http://dx.doi.org/10.1016/j.jnnfm.2009.03.014 en
heal.language English en
heal.publicationDate 2009 en
heal.abstract We develop a single segment differential tube model including interchain tube pressure effect (ITPE) [G. Marrucci, G. Ianniruberto, Interchain pressure effect in extensional flows of entangled polymers, Macromolecules 36 (2004) 3934-3942], able to describe the non-linear behaviour of entangled linear polymers. The model accounts for the effect of flow on the tube length and diameter. It is presented in two versions, depending on which tube dimension is assumed to deform affinely. The classical relaxation mechanisms, i.e., reptation, stretch dynamics, convective constraint release (CCR), as well as finite extensibility, are incorporated in a simple manner; hence the model allows an explicit comparison of the relative importance of various effects. A striking result is the insignificance of finite extensibility and the detrimental influence of CCR for moderately entangled systems when ITPE is taken into account. For highly entangled systems, CCR regains importance to avoid the well-known shear stress instability. The proposed model is able to make quantitative predictions of steady elongational and shear data for monodisperse melts, while transient values are less accurate but within experimental errors. (C) 2009 Elsevier B.V. All rights reserved. en
heal.publisher ELSEVIER SCIENCE BV en
heal.journalName Journal of Non-Newtonian Fluid Mechanics en
dc.identifier.doi 10.1016/j.jnnfm.2009.03.014 en
dc.identifier.isi ISI:000268939600002 en
dc.identifier.volume 161 en
dc.identifier.issue 1-3 en
dc.identifier.spage 10 en
dc.identifier.epage 18 en


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