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...
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Published in | Journal of food engineering Vol. 89; no. 4; pp. 441 - 447 |
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Main Authors | , , , |
Format | Journal Article |
Language | English |
Published |
Oxford
Elsevier Ltd
01.12.2008
[New York, NY]: Elsevier Science Pub. Co Elsevier |
Subjects | |
Online Access | Get full text |
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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. |
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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 |