Abstract

The present study experimentally investigates the effect of convergence angle of microchannel on two-phase flow and heat transfer during steam condensation. Three condensation regimes, from the inlet to the outlet, are identified: mist/annular flow, injection flow, and slug-bubbly flow. Flow pattern maps are constructed using superficial vapor and liquid velocities as the coordinates, wherein relatively distinct boundaries between the flow patterns can be identified. The experimental results show that the condensation heat flux increases with an increase in the convergence angle and/or the steam mass flux at a given coolant flow ratebut decreases with an increase in the coolant flow rate at a given steam mass flux. The results further demonstrate that the local condensation heat transfer coefficient in the mist/annular flow region is much higher than that in other condensation regimes. Moreover, the local condensation heat transfer coefficient in the mist/annular flow and injection flow region decreases with an increase in the convergence angle.

Highlights

  • Condensation in microchannels is of significant fundamental interest and has diversified applications, such as in microchannel heat exchangers and micro-fuel cells

  • Condensation two-phase flow patterns in microchannels have been investigated in many studies

  • More detailed discussions on the characteristics of condensation two-phase flow pattern in rectangular microchannels with different cross-section designs have been presented in our previous study [14]

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Summary

Introduction

Condensation in microchannels is of significant fundamental interest and has diversified applications, such as in microchannel heat exchangers and micro-fuel cells. Wu and Cheng [1] visualized the condensation flow patterns of steam flowing through 10 parallel microchannels with a hydraulic diameter of 82.8 μm and a trapezoidal cross-sectional area. They categorized the flow patterns observed as follows: droplet flow (mist flow), annular flow, injection flow, and slug-bubbly flow. Wu et al [2] further carried out experimental studies on injection flow during steam condensation in microchannels with hydraulic diameters ranging from 53 μm to 128.5 μm. They proposed that the location of the injection flow corresponds to the Reynolds number (Re), condensation number (Co), and diameter-to-length ratio (Dh/L) and obtained a dimensionless correlation for the location of injection flow in silicon microchannels

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