<?xml version="1.0" encoding="UTF-8"?><?xml-stylesheet type="text/xsl" href="static/style.xsl"?><OAI-PMH xmlns="http://www.openarchives.org/OAI/2.0/" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xsi:schemaLocation="http://www.openarchives.org/OAI/2.0/ http://www.openarchives.org/OAI/2.0/OAI-PMH.xsd"><responseDate>2026-05-29T20:33:42Z</responseDate><request verb="GetRecord" identifier="oai:riuma.uma.es:10630/33558" metadataPrefix="oai_dc">https://riuma.uma.es/rest/oai/request</request><GetRecord><record><header><identifier>oai:riuma.uma.es:10630/33558</identifier><datestamp>2026-02-03T11:09:03Z</datestamp><setSpec>com_10630_2254</setSpec><setSpec>col_10630_37953</setSpec></header><metadata><oai_dc:dc xmlns:dc="http://purl.org/dc/elements/1.1/" xmlns:doc="http://www.lyncode.com/xoai" xmlns:oai_dc="http://www.openarchives.org/OAI/2.0/oai_dc/" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xsi:schemaLocation="http://www.openarchives.org/OAI/2.0/oai_dc/ http://www.openarchives.org/OAI/2.0/oai_dc.xsd">
   <dc:title>Dynamics of viscoelastic pipe flow at low Reynolds numbers in the maximum drag reduction limit</dc:title>
   <dc:creator>López-Alonso, José Manuel</dc:creator>
   <dc:creator>Choueiri, George H.</dc:creator>
   <dc:creator>Hof, Björn</dc:creator>
   <dc:subject>Flujos (Sistemas dinámicos diferenciables)</dc:subject>
   <dc:subject>Elasto-inertial instability</dc:subject>
   <dc:subject>Viscoelastic pipe flow</dc:subject>
   <dc:subject>Direct numerical simulations</dc:subject>
   <dc:subject>FENEP model</dc:subject>
   <dc:description>Polymer additives can substantially reduce the drag of turbulent flows and the upper limit, the so-called state of ‘maximum drag reduction’ (MDR), is to a good approximation independent of the type of polymer and solvent used. Until recently, the consensus was that, in this limit, flows are in a marginal state where only a minimal level of turbulence activity persists. Observations in direct numerical simulations at low Reynolds numbers ( Re&#xd;
 ) using minimal sized channels appeared to support this view and reported long ‘hibernation’ periods where turbulence is marginalized. In simulations of pipe flow at  Re&#xd;
  near transition we find that, indeed, with increasing Weissenberg number ( Wi&#xd;
 ), turbulence expresses long periods of hibernation if the domain size is small. However, with increasing pipe length, the temporal hibernation continuously alters to spatio-temporal intermittency and here the flow consists of turbulent puffs surrounded by laminar flow. Moreover, upon an increase in  Wi&#xd;
 , the flow fully relaminarizes, in agreement with recent experiments. At even larger  Wi&#xd;
 , a different instability is encountered causing a drag increase towards MDR. Our findings hence link earlier minimal flow unit simulations with recent experiments and confirm that the addition of polymers initially suppresses Newtonian turbulence and leads to a reverse transition. The MDR state on the other hand results at these low Re&#xd;
  from a separate instability and the underlying dynamics corresponds to the recently proposed state of elasto-inertial turbulence.</dc:description>
   <dc:date>2024-09-27T06:53:12Z</dc:date>
   <dc:date>2024-09-27T06:53:12Z</dc:date>
   <dc:date>2024-09-20</dc:date>
   <dc:date>2019-07-12</dc:date>
   <dc:type>journal article</dc:type>
   <dc:type>AM</dc:type>
   <dc:identifier>Lopez JM, Choueiri GH, Hof B. Dynamics of viscoelastic pipe flow at low Reynolds numbers in the maximum drag reduction limit. Journal of Fluid Mechanics. 2019;874:699-719. doi:10.1017/jfm.2019.486</dc:identifier>
   <dc:identifier>https://hdl.handle.net/10630/33558</dc:identifier>
   <dc:identifier>10.1017/jfm.2019.486</dc:identifier>
   <dc:language>eng</dc:language>
   <dc:rights>open access</dc:rights>
   <dc:format>application/pdf</dc:format>
   <dc:publisher>Cambridge University Press</dc:publisher>
</oai_dc:dc>
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