1996
DOI: 10.1016/s0017-9310(96)85013-7
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Investigation of flow and heat transfer in corrugated passages—I. Experimental results

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Cited by 158 publications
(59 citation statements)
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“…Due to the broad range of application of this heat transfer equipment, several experimental and modelling works have been performed in order to study the thermal and hydraulic performance of different plate patterns, fouling tendency, corrosion mechanisms and the optimization of different arrangements and configurations, when leading with Newtonian or non-Newtonian fluids (Afonso et al, 2003;Antonini, François, & Shuai, 1987;Bassiouny & Martin, 1984;Delplace & Leuliet, 1995;Gut & Pinto, 2003a, 2003bKho & Mü ller-Steinhagen, 1999;Leuliet, Maigonnat, & Lalande, 1987, 1988, 1990Mehrabian & Poulter, 2000;Metwally & Manglick, 2004;Stasiek, Collins, Ciofalo, & Chew, 1996).…”
Section: Introductionmentioning
confidence: 99%
“…Due to the broad range of application of this heat transfer equipment, several experimental and modelling works have been performed in order to study the thermal and hydraulic performance of different plate patterns, fouling tendency, corrosion mechanisms and the optimization of different arrangements and configurations, when leading with Newtonian or non-Newtonian fluids (Afonso et al, 2003;Antonini, François, & Shuai, 1987;Bassiouny & Martin, 1984;Delplace & Leuliet, 1995;Gut & Pinto, 2003a, 2003bKho & Mü ller-Steinhagen, 1999;Leuliet, Maigonnat, & Lalande, 1987, 1988, 1990Mehrabian & Poulter, 2000;Metwally & Manglick, 2004;Stasiek, Collins, Ciofalo, & Chew, 1996).…”
Section: Introductionmentioning
confidence: 99%
“…At lower heat transfer coefficient, the discrepancy may have been caused by two reasons. One is the simplification of a lumped fluid heat transfer coefficient, as the heat transfer coefficient in unitary cell has been shown to vary by experiment [21][22] and CFD model [22][23]. The other reason is that the experimental data only represents an averaged value of the entire heat exchanger.…”
Section: Effect Of End Plate On Heat Transfermentioning
confidence: 99%
“…In the present study, the fin shape is determined following Utriainen and Sunden 18) and the fin height is set to 4 mm based on a design study by Sumitomo Precision Products. 19) The heat transfer coefficient h and friction factor f of the fin are estimated from experiment of Stasiek et al 20) as follows.…”
Section: Heat Exchanger Modelmentioning
confidence: 99%