4.7 Article

Experimental investigation on thermo-hydraulic performance of triangular cross-corrugated flow passages

Publisher

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.icheatmasstransfer.2021.105160

Keywords

Corrugated passages; Heat exchangers; Pressure drop; Friction factor; Nusselt number

Funding

  1. College of Engineering and Postdoctoral Studies of the University of Saskatchewan
  2. National Science and Engineering Research Council (NSERC), Canada
  3. Tempeff North America Inc., Winnipeg, Canada [533225-18]

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This paper experimentally investigates the heat transfer and pressure drop characteristics of triangular-shaped cross-corrugated flow passages and provides correlations for the average Nusselt number and friction factor, which will be useful for manufactures and designers in developing high-performance heat exchangers.
Heat exchangers made of corrugated flow passages generally have better thermo-hydraulic performance compared to parallel flow passages. The corrugation angle (beta), corrugation pattern, and the ratio of depth to pitch (h(ch)/P-ch) are critical geometrical parameters influencing the heat transfer and pressure drop in corrugated flow passages. This paper experimentally investigates heat transfer and pressure drop characteristics of triangular-shaped cross-corrugated flow passages for the range of 25. < beta < 75. and 0.13 < h(ch)/P-ch < 0.36. Experiments are performed using representative compact heat exchangers in a small-scale test facility. This study also reports the effects of plate geometry on heat transfer and pressure drop and provides correlations for the average Nusselt number and friction factor. A detailed comparison of test data with relevant literature is also presented. Results of this study will be useful to manufactures and designers for developing high-performance heat exchangers.

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