2008
DOI: 10.1016/j.jfoodeng.2008.05.022
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Friction factors of power-law fluids in chevron-type plate heat exchangers

Abstract: a b s t r a c tIn the present work laminar flows of Newtonian and power-law fluids through cross-corrugated chevrontype 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, b, 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 b by developing an adequate definiti… Show more

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Cited by 28 publications
(18 citation statements)
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“…The confocal micro-PIV system was first evaluated by comparing the experimental results not only with a well established analytical solution for steady flow in a rectangular microchannel [15] but also with a reliable numerical method that was used in past investigations to study the flow behaviour of Newtonian or non-Newtonian fluids at low Reynolds numbers [9,10]. The numerical, experimental and analytical results of the present work were obtained for the middle plane (25 m height) of the rectangular microchannel.…”
Section: Resultsmentioning
confidence: 99%
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“…The confocal micro-PIV system was first evaluated by comparing the experimental results not only with a well established analytical solution for steady flow in a rectangular microchannel [15] but also with a reliable numerical method that was used in past investigations to study the flow behaviour of Newtonian or non-Newtonian fluids at low Reynolds numbers [9,10]. The numerical, experimental and analytical results of the present work were obtained for the middle plane (25 m height) of the rectangular microchannel.…”
Section: Resultsmentioning
confidence: 99%
“…The size of the elements was fixed after a grid independence test. The grids were successively refined and the velocity obtained with the different meshes were compared, the results being considered independent of the mesh when a difference bellow 1% was achieved [4,[8][9][10].…”
Section: Simulation Methodsmentioning
confidence: 99%
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“…The pressure drops due to bend, sudden contraction and sudden expansion at inlet and outlets, respectively, have been calculated by using the following formula: (6) Where is the total pressure loss coefficient of the bend, sudden contraction and sudden expansion at the inlet and outlet of the ports. The pressure drop due to friction in the small steel connecting pipe at the inlet and outlet of the plate heat exchanger was estimated on the basis of the smooth steel tube friction factor and pipe flow velocity as (7) The pressure drop due to friction in the corrugated passage is calculated based on the flow rate by using an empirical formula:…”
Section: Mathematical Analysismentioning
confidence: 99%
“…The studied low corrugation angle plates have been used for different number of channels, namely, 20 and 80. Fernandes et al [6] have been numerically studied the geometry of the channels for laminar flows of Newtonian and power-law fluids through cross-corrugated chevron type plate heat exchangers (PHEs). The plates area enlargement factor was a typical one (1.17), the corrugation angle, β, varied between 30 and 60 and the flow index behavior, n, between 0.25 and 1.…”
Section: Introductionmentioning
confidence: 99%