Abstract:
The process of heat transfer at pool boiling of liquid (Freon R21) on tubes with three-dimensional plasma-deposited capillary-porous coatings of various thicknesses has been experimentally studied. Comparative analysis of experimental data showed that the heat transfer coefficient for a heater tube with a 500-$\mu$m-thick porous coating is more than twice as large as that in liquid boiling on an otherwise similar uncoated tube. At the same time, no intensification of heat exchange in the regime of bubble boiling is observed on a tube with a 100-$\mu$m-thick porous coating.
Keywords:Heat Transfer, Heat Transfer Coefficient, Heat Transfer Rate, Technical Physic Letter, Heat Flux Density.