Heat Transfer in Liquid Film Falling Down Vertical Cylinder with Single-Layer and Gradient Two-Layer Mesh Coatings
dc.contributor.author | Volodin O.A.; Pecherkin N.I.; Konev S.V.; Das M.K.; Pavlenko A.N. | en_US |
dc.date.accessioned | 2025-02-17T11:12:59Z | |
dc.date.issued | 2024 | |
dc.description.abstract | Abstract: The paper presents the results of a study of heat transfer in laminar-wave liquid films falling down the outer surface of a vertical cylinder. As intensifiers of heat transfer during boiling, single-layer micromesh coatings with different geometric characteristics and a two-layer gradient mesh coating were used. The working liquid was mixture of refrigerants R114-R21 with the initial concentration of the low-boiling component (R114) equal to 12%. The film Reynolds number at the entrance to the test section varied from 400 to 1300; the heat flux density varied in the range of 0�6�W/cm2. The results of measuring the heat transfer coefficients in the regimes of evaporation and nucleate boiling of the film are presented. A comparison is made of the results obtained on the single-layer and two-layer mesh coatings, as well as with previously obtained data for a combined coating (created by the method of deformational cutting in combination with a mesh coating). It has been shown that, in comparison with the smooth surface, the heat transfer coefficient during boiling of the falling film can be increased up to 2�times with the single-layer mesh coating and up to 1.7�times with the two-layer gradient mesh coating. � Pleiades Publishing, Ltd. 2024. | en_US |
dc.identifier.citation | 0 | en_US |
dc.identifier.uri | http://dx.doi.org/10.1134/S1810232824020036 | |
dc.identifier.uri | https://idr.iitbbs.ac.in/handle/2008/5110 | |
dc.language.iso | en | en_US |
dc.title | Heat Transfer in Liquid Film Falling Down Vertical Cylinder with Single-Layer and Gradient Two-Layer Mesh Coatings | en_US |
dc.type | Article | en_US |