4.4 Article

Lattice Boltzmann investigation of flow boiling in a microchannel

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SAGE PUBLICATIONS LTD
DOI: 10.1177/09544062221089144

关键词

Lattice Boltzmann; flow boiling; heat transfer; microchannel; numerical methods and simulations

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In this study, a hybrid multiphase lattice Boltzmann model is used to investigate flow boiling heat transfer in a horizontal microchannel. The flow pattern transition is reproduced by varying the heat flux, and the effects of liquid mass flux, heating wall wettability, and channel confinement height on bubble dynamics and heat transfer performance are discussed. The results show that a sequence of flow patterns occurs in the microchannel with increasing heat flux, and the dominant heat transfer mechanism varies accordingly. Increasing mass flux or confinement height extends the range of high-efficiency flow patterns. A hydrophilic heating wall is preferred for better heat transfer performance in the microchannel.
A hybrid multiphase lattice Boltzmann model is adopted to investigate the flow boiling heat transfer process in a horizontal microchannel with consideration of bubble dynamics. The flow pattern transition in a microchannel, involving single-phase flow, bubbly flow, slug flow, and contact-slug flow, is reproduced by varying the heat flux. The influencing parameters, including the liquid mass flux, the heating wall wettability, and the confinement height of channels, on dynamic bubble behaviors and heat transfer performance are discussed. The results indicate that a sequence of single-phase flow, bubbly flow, slug flow, and contact-slug flow occurs in a microchannel with increasing heat flux. Correspondingly, the dominant heat transfer mechanism experiences the liquid convection (single-phase flow), nucleate boiling (bubbly flow), the microlayer evaporation (slug flow), and the hybrid gas convection and microlayer evaporation (contact-slug flow). The increase of mass flux or confinement height extends the range of heat flux for high-efficiency bubbly and slug flow. The hydrophilic heating wall is preferred for better heat transfer performance in a microchannel due to the strengthened microlayer evaporation and less vapor occupation of the effective nucleation area.

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