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Influence of surface structure and tube material on the condensation heat transfer coefficient of n-butane on horizontal single tubes and in tube bundles.

Authors :
Kühl, Julius V.W.
Palm, Franz G.
Dietl, Jochen
El-Hajal, Jean
Gotterbarm, Achim
Rausch, Michael H.
Klein, Tobias
Fröba, Andreas P.
Source :
International Journal of Heat & Mass Transfer. Nov2024, Vol. 233, pN.PAG-N.PAG. 1p.
Publication Year :
2024

Abstract

• n -butane is investigated as refrigerant with low global warming potential. • single tube and tube bundle experiments for smooth and finned condensation tubes. • variation of fin density and fin height for copper and cooper/nickel tubes. • analytical prediction model is tested for a large variation of finned tubes. The present study examines the condensation heat transfer coefficient α cond of n -butane on the outside of different horizontal tubes and in corresponding tube bundles. Experiments were conducted with a smooth tube, finned tubes with various fin densities, fin heights and tube materials, and a high-performance condensation tube (HPT) at vapor temperatures of (40 and 78) °C and varying heat flux densities q̇. The influence of inundation on α cond was systematically investigated by varying the mass flow of liquid condensate at q̇ of (20 and 60) kW· m −2. Differences between the experimental results from this work and previous ones for propane on the same condensation tubes could be explained with the help of the thermophysical properties and, thus, the retention angle of the condensate in the channels between the fins and the condensate layer thickness. For single copper tubes, α cond increased with increasing fin densities from (19 to 48) fins per inch and was between 9 and 17 times larger than for the smooth tube. This enhancement factor even reached a value of about 24 for the HPT. These increases can be attributed in part to the increased surface area, but the strongest effect appears to be related to surface tension-driven drainage of the condensate. In addition to the experimental investigations, α cond of the finned condensation tubes was predicted using an analytical model for the condensation heat transfer on finned tubes. Here, excellent agreement with an average deviation from the experimental results of 6.6 % could be found. Studies of the inundation effect have shown that the expected decrease in α cond due to the additional condensate impinging on the tubes inside bundles and increasing the film thickness often holds, but is partially counteracted by other effects and depends on the tube geometry. [ABSTRACT FROM AUTHOR]

Details

Language :
English
ISSN :
00179310
Volume :
233
Database :
Academic Search Index
Journal :
International Journal of Heat & Mass Transfer
Publication Type :
Academic Journal
Accession number :
179172530
Full Text :
https://doi.org/10.1016/j.ijheatmasstransfer.2024.125973