4.7 Article

Condensation heat transfer in annuli outside horizontal stainless steel enhanced tubes

期刊

出版社

ELSEVIER FRANCE-EDITIONS SCIENTIFIQUES MEDICALES ELSEVIER
DOI: 10.1016/j.ijthermalsci.2022.107479

关键词

Outside tube condensation; R410A; Enhanced heat transfer (EHT); Correlation

资金

  1. National Science Foundation of China [52076187]
  2. Science and Technology on Thermal Energy and Power Laboratory Open Foundation of China [TPL2022B04]

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Condensation heat transfer of R410A outside several enhanced heat transfer tubes (dimple/herringbone, herringbone, and dimple) and smooth tube was evaluated. The study found that the herringbone tube effectively improved the flow condensation performance outside the tubes, while the dimple-only structure was ineffective. The composite surface, produced by combining dimple and herringbone microfin patterns, showed substantial enhancement due to the liquid drainage effects and turbulence caused by the two structures.
The condensation heat transfer of R410A outside several enhanced heat transfer (EHT) tubes [dimple/herringbone (DIM/HB), herringbone (HB), and dimple (DIM)] and smooth tube were evaluated. All tubes are made of stainless steel; the test length is 2 m; the outer diameter is 12.7 mm; the inner diameter is 11.5 mm. Experimental conditions were set at a saturated temperature of 45 ?; condensed vapor mass decreased from 0.8 to 0.2; mass flux ranged between 75 and 225 kg m(-2) s(-1). As a result, the HB tube effectively improved flow condensation performance outside tubes; while the dimple-only structure is not effective since it produces a lower heat transfer coefficient (HTC) than a smooth tube (at some low flow rate conditions). Substantial enhancement is produced by the DIM/HB composite surface produced from dimple and herringbone microfin patterns, which is due to the combination of the liquid drainage effects by herringbone structure to remove condensate and causing strong turbulence of dimple structure. With the increase of mass flux and average vapor quality, the condensation heat transfer coefficient and pressure drop of each test tube increase as well. Additionally, an improved Nusselt equation for external condensation on a smooth tube was developed to predict the heat transfer coefficient for the experimental conditions considered here. Finally, correlations of enhanced heat transfer (EHT) tubes (microfin - HB, dimple -DIM, and composite surface - DIM/HB) to predict condensation heat transfer coefficient were developed and evaluated.

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