Friction factors of power-law fluids in chevron-type plate heat exchangers

In the present work laminar flows of Newtonian and power-law fluids through cross-corrugated chevron-type plate heat exchangers (PHEs) are numerically studied in terms of the geometry of the channels. The plates area enlargement factor was a typical one (1.17), the corrugation angle, β, varied betwe...

Full description

Saved in:
Bibliographic Details
Published inJournal of food engineering Vol. 89; no. 4; pp. 441 - 447
Main Authors Fernandes, Carla S., Dias, Ricardo P., Nóbrega, João M., Maia, João M.
Format Journal Article
LanguageEnglish
Published Oxford Elsevier Ltd 01.12.2008
[New York, NY]: Elsevier Science Pub. Co
Elsevier
Subjects
Online AccessGet full text

Cover

Loading…
More Information
Summary:In the present work laminar flows of Newtonian and power-law fluids through cross-corrugated chevron-type plate heat exchangers (PHEs) are numerically studied in terms of the geometry of the channels. The plates area enlargement factor was a typical one (1.17), the corrugation angle, β, varied between 30° and 60° and the flow index behaviour, n, between 0.25 and 1. Single friction curves fRe g = K for both Newtonian and non-Newtonian fluids are proposed for each β by developing an adequate definition of the generalised Reynolds number, Re g. The coefficient K compares well with experimental data, for all (seven) values of β, and depends on the tortuosity coefficient, τ. It was found that, for each β, τ decreases with the decrease of n. Food fluids are frequently processed in PHEs and usually behave as non-Newtonian fluids. This study can be useful in engineering applications as well as in the characterization of transport phenomena in PHEs.
Bibliography:http://dx.doi.org/10.1016/j.jfoodeng.2008.05.022
ObjectType-Article-2
SourceType-Scholarly Journals-1
ObjectType-Feature-1
content type line 23
ISSN:0260-8774
1873-5770
DOI:10.1016/j.jfoodeng.2008.05.022