This article presents the results of experimental investigation of heat transfer process, carried out using the model of heat exchanger. Two-phase statically stable foam flow was used as a heat transfer fluid. Heat exchanger model consisted of staggered tube bank. Experimental results are presented with the focus on influence of tube position in the line of the bank, volumetric void faction and velocity of gas component of the foam. The phenomena of liquid draining in cellular foam flow and its influence on heat transfer rate has also been discussed. The experimental results have been generalized by relationship between Nusselt, Reynolds and Prandtl numbers.
JAKUBCIONIS Mindaugas;
2015-07-28
SCIENCE PRESS
JRC95549
1003-2169,
http://link.springer.com/article/10.1007/s11630-015-0783-1,
https://publications.jrc.ec.europa.eu/repository/handle/JRC95549,
10.1007/s11630-015-0783-1,
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