Nucleate boiling of non-Newtonian fluids in a stirred tank reactor
Identifieur interne : 000F85 ( PascalFrancis/Curation ); précédent : 000F84; suivant : 000F86Nucleate boiling of non-Newtonian fluids in a stirred tank reactor
Auteurs : L. Floquet-Muhr [France] ; N. MidouxSource :
- Chemical engineering and processing [ 0255-2701 ] ; 1994.
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- Pascal (Inist)
English descriptors
- KwdEn :
Abstract
The nucleate boiling of non-Newtonian fluids has been investigated in a mechanically stirred tank. The wall heated reactor is stirred with an anchor. The case of high consistency fluids has been more specifically studied. It was shown that when the fluid consistency increases, the predominant mechanisms of boiling heat transfer change, resulting in the fact that the correlations which can be used as a design estimate for low viscosity fluids cannot be used any more. A method was proposed for these fluids to estimate nucleate flow boiling heat transfer from the forced convection predictions
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Pascal:95-0045223Le document en format XML
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<author><name sortKey="Floquet Muhr, L" sort="Floquet Muhr, L" uniqKey="Floquet Muhr L" first="L." last="Floquet-Muhr">L. Floquet-Muhr</name>
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<country>France</country>
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<author><name sortKey="Midoux, N" sort="Midoux, N" uniqKey="Midoux N" first="N." last="Midoux">N. Midoux</name>
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<author><name sortKey="Midoux, N" sort="Midoux, N" uniqKey="Midoux N" first="N." last="Midoux">N. Midoux</name>
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<series><title level="j" type="main">Chemical engineering and processing</title>
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<term>Heat transfer</term>
<term>Modeling</term>
<term>Non Newtonian fluid</term>
<term>Nucleate boiling</term>
<term>Pseudoplastic fluid</term>
<term>Stirred tank reactor</term>
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<keywords scheme="Pascal" xml:lang="fr"><term>Réacteur agité</term>
<term>Ebullition nucléée</term>
<term>Fluide non newtonien</term>
<term>Fluide pseudoplastique</term>
<term>Transfert chaleur</term>
<term>Modélisation</term>
<term>Etude expérimentale</term>
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<front><div type="abstract" xml:lang="en">The nucleate boiling of non-Newtonian fluids has been investigated in a mechanically stirred tank. The wall heated reactor is stirred with an anchor. The case of high consistency fluids has been more specifically studied. It was shown that when the fluid consistency increases, the predominant mechanisms of boiling heat transfer change, resulting in the fact that the correlations which can be used as a design estimate for low viscosity fluids cannot be used any more. A method was proposed for these fluids to estimate nucleate flow boiling heat transfer from the forced convection predictions</div>
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<fA21><s1>1994</s1>
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<fC01 i1="01" l="ENG"><s0>The nucleate boiling of non-Newtonian fluids has been investigated in a mechanically stirred tank. The wall heated reactor is stirred with an anchor. The case of high consistency fluids has been more specifically studied. It was shown that when the fluid consistency increases, the predominant mechanisms of boiling heat transfer change, resulting in the fact that the correlations which can be used as a design estimate for low viscosity fluids cannot be used any more. A method was proposed for these fluids to estimate nucleate flow boiling heat transfer from the forced convection predictions</s0>
</fC01>
<fC01 i1="02" l="FRE"><s0>L'ébullition nucléee de fluides non newtoniens a été étudiée en réacteur agité. Le réacteur utilisé est chauffé à la paroi et le mobile d'agitation est une ancre. Le cas de fluides ayant une consistance élevée a plus spécifiquement été considéré. On a observé que lorsque la consistance du fluide augmente, les mécanismes prédominants dont dépend le transfert thermique en ébullition changent; les relations utilisées à faible viscosité pour évaluer le flux thermique en ébullition nucléée et agitée ne sont alors plus adéquates. Une méthode a été proposée pour ces fluides pour estimer le flux thermique en ébullition nucléée et agitée à l'aide des corrélations de la convection forcée</s0>
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<s5>01</s5>
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<s5>01</s5>
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<s5>02</s5>
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<fC03 i1="02" i2="X" l="ENG"><s0>Nucleate boiling</s0>
<s5>02</s5>
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<s5>02</s5>
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<fC03 i1="03" i2="X" l="FRE"><s0>Fluide non newtonien</s0>
<s5>03</s5>
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<s5>03</s5>
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<s5>04</s5>
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<s5>05</s5>
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<s5>05</s5>
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<s5>06</s5>
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<fC03 i1="07" i2="X" l="FRE"><s0>Etude expérimentale</s0>
<s5>07</s5>
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<fC03 i1="07" i2="X" l="ENG"><s0>Experimental study</s0>
<s5>07</s5>
</fC03>
<fC03 i1="07" i2="X" l="GER"><s0>Experimentelle Untersuchung</s0>
<s5>07</s5>
</fC03>
<fC03 i1="07" i2="X" l="SPA"><s0>Estudio experimental</s0>
<s5>07</s5>
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<fN21><s1>039</s1>
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