Abstract

The phenomena of microlayer formation and its dynamic characteristics during the nucleate pool boiling regime have been widely investigated in the past. However, experimental works on real-time microlayer dynamics during nucleate flow boiling conditions are highly scarce. The present work is an attempt to address this lacuna and is concerned with developing a fundamental understanding of microlayer dynamics during the growth process of a single vapour bubble under nucleate flow boiling conditions. Boiling experiments have been conducted under subcooled conditions in a vertical rectangular channel with water as the working fluid. Thin-film interferometry combined with high-speed cinematography have been adopted to simultaneously capture the dynamic behaviour of the microlayer along with the bubble growth process. Transients associated with the microlayer have been recorded in the form of interferometric fringe patterns, which clearly reveal the evolution of the microlayer beneath the growing vapour bubble, the movement of the triple contact line and the growth of the dryspot region during the bubble growth process. While symmetric growth of the microlayer was confirmed in the early growth phase, the bulk flow-induced bubble deformation rendered asymmetry to its profile during the later stages of the bubble growth process. The recorded fringe patterns have been quantitatively analysed to obtain microlayer thickness profiles at different stages of the bubble growth process. ForRe = 3600, the maximum thickness of the almost wedge-shaped microlayer was obtained asδ ~ 3.5 μm for a vapour bubble of diameter 1.6 mm. Similarly, forRe = 6000, a maximum microlayer thickness ofδ ~ 2.5 μm was obtained for a bubble of diameter 1.1 mm.

Highlights

  • Boiling has been proven to be one of the most efficient modes of heat transfer

  • Initial microlayer thickness has been calculated and compared with empirical and theoretical models available in the literature. In addition to these parameters, the experimental observation of microlayer dynamics has been employed to elucidate the possible role(s) of various heat transfer mechanisms that contribute towards the overall bubble growth process under flow boiling conditions

  • When the indium tin oxide (ITO) heater is connected to the electrical supply, local resistance to current flow increases in the neck region, which leads to a relative increase in the temperature compared to the other locations of the heater and helps to achieve the threshold temperature required for the onset of nucleation in the neck region

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Summary

Introduction

Boiling has been proven to be one of the most efficient modes of heat transfer. Two widely accepted heat transfer mechanisms explain the enhanced heat transfer rates associated with nucleate boiling as micro-convection and microlayer evaporation. Microlayer dynamics during growth of a vapour bubble (2018) measured microlayer thickness and bubble volume simultaneously using laser interferometry and high-speed videography during nucleate pool boiling of water and ethanol. Narayan L & Srivastava (2021a) performed pool boiling experiments to understand the intricate relation between heat transfer processes through the microlayer and superheated liquid layer and transient conduction by simultaneously capturing the microlayer formation and thermal field around a single vapour bubble using synchronized thin-film interferometry and rainbow schlieren deflectometry. Initial microlayer thickness has been calculated and compared with empirical and theoretical models available in the literature In addition to these parameters, the experimental observation of microlayer dynamics has been employed to elucidate the possible role(s) of various heat transfer mechanisms that contribute towards the overall bubble growth process under flow boiling conditions

Experimental apparatus
Results and discussion
Dynamics of microlayer and vapour bubble
Initial microlayer thickness
Role of microlayer evaporation towards bubble growth
Conclusions
Full Text
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