The impacts of gas-liquid two-phase flow regimes on heat transfer performance and pressure drop in microchannels-an experimental study

The two-phase flow regimes have significant effects on pressure drop and performances of heat transfer. There are few studies on the heat transfer of non-boiling two-phase flow in silicon microchannels. The gas-water two-phase flows is highly influenced by surface configurations. Here, a novel nanoengineered microchannel design, names as nanofenced microchannel, was proposed to rectify the disordered two-phase flows into annular flow. This supercapillary nanofence can dramatically boost the liquid spreading along the side walls that can favor the thin film evaporation. Also, two-phase flow instabilities might be significantly reduced upon establishment of annular flow. In this work, Nitrogen gas (N 2 ) and water two-phase flows are experimental studied in parallel five microchannels. The dimensions of each channel are W = 220 μm, H = 250 μm, L = 10 mm, respectively. The gap between the nanofence and sidewall is 5 μm. The height of nanofence is 100 μm. The performances of heat transfer and pressure drop are investigated with water superficial velocity varying from 0.06 m/s to 0.6 m/s under a constant heat flux of 30 W/cm 2 . The N 2 quality ranges from 0.0025 to 0.3. Bubbly, slug, slug/annular and annular flow patterns were observed by changing the N 2 quality. The results demonstrate that the heat transfer performance in nanofenced microchannels is significantly enhanced, accompanying with the decrease of two-phase pressure drop, reduced by 15 % at moderate water flow rates. However, it increases at high water superficial velocity by 20 %. Transient results show that performances of heat transfer and pressure drop are close related to two-phase flow patterns. • A nanoengineered microchannel was proposed to rectify the disordered two-phase flows. • The impacts of gas-liquid two-phase flow regimes on heat transfer performance were experimentally studied. • Bubbly, slug, slug/annular and annular flow patterns were observed by changing the N 2 quality. • Convective heat transfer performance in nanofenced microchannels is significantly enhanced.

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Publication Details

Journal
International Journal of Thermal Sciences
Published
2025-08-13
DOI
https://doi.org/10.1016/j.ijthermalsci.2025.110232
Citations
3
Primary Topic
Heat Transfer and Boiling Studies
Type
article
Field-Weighted Citation Impact
2.14

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article

The impacts of gas-liquid two-phase flow regimes on heat transfer performance and pressure drop in microchannels-an experimental study

Jingwei Han, Wenming Li, Guanghan Huang, Shan Li
3 citations
International Journal of Thermal Sciences
Heat Transfer and Boiling Studies
2.14
article

The impacts of gas-liquid two-phase flow regimes on heat transfer performance and pressure drop in microchannels-an experimental study

Jingwei Han, Wenming Li, Guanghan Huang, Shan Li
article en
3 citations

Abstract

The two-phase flow regimes have significant effects on pressure drop and performances of heat transfer. There are few studies on the heat transfer of non-boiling two-phase flow in silicon microchannels. The gas-water two-phase flows is highly influenced by surface configurations. Here, a novel nanoengineered microchannel design, names as nanofenced microchannel, was proposed to rectify the disordered two-phase flows into annular flow. This supercapillary nanofence can dramatically boost the liquid spreading along the side walls that can favor the thin film evaporation. Also, two-phase flow instabilities might be significantly reduced upon establishment of annular flow. In this work, Nitrogen gas (N 2 ) and water two-phase flows are experimental studied in parallel five microchannels. The dimensions of each channel are W = 220 μm, H = 250 μm, L = 10 mm, respectively. The gap between the nanofence and sidewall is 5 μm. The height of nanofence is 100 μm. The performances of heat transfer and pressure drop are investigated with water superficial velocity varying from 0.06 m/s to 0.6 m/s under a constant heat flux of 30 W/cm 2 . The N 2 quality ranges from 0.0025 to 0.3. Bubbly, slug, slug/annular and annular flow patterns were observed by changing the N 2 quality. The results demonstrate that the heat transfer performance in nanofenced microchannels is significantly enhanced, accompanying with the decrease of two-phase pressure drop, reduced by 15 % at moderate water flow rates. However, it increases at high water superficial velocity by 20 %. Transient results show that performances of heat transfer and pressure drop are close related to two-phase flow patterns. • A nanoengineered microchannel was proposed to rectify the disordered two-phase flows. • The impacts of gas-liquid two-phase flow regimes on heat transfer performance were experimentally studied. • Bubbly, slug, slug/annular and annular flow patterns were observed by changing the N 2 quality. • Convective heat transfer performance in nanofenced microchannels is significantly enhanced.

International Journal of Thermal SciencesVol. 219
Guangdong University of Technology (CN), Southeast University (CN)
National Natural Science Foundation of China, Basic and Applied Basic Research Foundation of Guangdong Province
Affordable and clean energy
Openalex Percentile: Top 13%
Heat Transfer and Boiling Studies
2.14
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