Abstract

To overcome the two-phase flow instability of traditional boiling heat dissipation technologies, a porous wick was used for liquid-vapor isolation, achieving efficient and stable boiling heat dissipation. A pump-assisted capillary phase-change loop with methanol as the working medium was established to study the effect of liquid-vapor pressure difference and heating power on its start-up and steady-state characteristics. The results indicated that the evaporator undergoes four heat transfer modes, including flooded, partially flooded, thin-film evaporation, and overheating. The thin-film evaporation mode was the most efficient with the shortest start-up period. In addition, heat transfer modes were determined by the liquid-vapor pressure difference and power. The heat transfer coefficient significantly improved and the thermal resistance was reduced by increasing liquid-vapor pressure as long as it did not exceed 8 kPa. However, when the liquid-vapor pressure exceeded 8 kPa, its influence on the heat transfer coefficient weakened. In addition, a two-dimensional heat transfer mode distribution diagram concerning both liquid-vapor pressure difference and power was drawn after a large number of experiments. During an engineering application, the liquid-vapor pressure difference can be controlled to maintain efficient thin-film evaporation in order to achieve the optimum heat dissipation effect.

Highlights

  • The heat transfer coefficient of phase-change heat dissipation is 1–2 orders of magnitude higher than single-phase convection heat dissipation

  • By establishing a pump-assisted capillary phase-change loop system with methanol as the working medium, this paper studies the effect of liquid-vapor pressure difference on both sides of the capillary wick on the start-up characteristics and steady-state heat transfer characteristics

  • The start-up characteristics of a pump-assisted capillary phase-change loop under liquidvapor pressure differences ∆pLV = 0, 2, 4, 6, 8, and 16 kPa are shown in Figure 3a–f, respectively

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Summary

Introduction

The heat transfer coefficient of phase-change heat dissipation is 1–2 orders of magnitude higher than single-phase convection heat dissipation. The alternate flow of liquid/vapor/liquid-vapor under high heat flux and low mass flux may cause strong pulsation, with a pressure fluctuation amplitude of up to 44 kPa and a temperature fluctuation of up to 229 ◦C This shows there are many types of two-phase flow instability in the phase-change cooling system, which are closely related to the transition of flow patterns. By establishing a pump-assisted capillary phase-change loop system with methanol as the working medium, this paper studies the effect of liquid-vapor pressure difference on both sides of the capillary wick on the start-up characteristics and steady-state heat transfer characteristics. The heating power was 10–81 W, and the liquid-vapor pressure difference was 0–22 kPa

Measurement and Uncertainty
Start-Up Characteristics
Steady-State Heat Transfer Characteristics
Baseplate Temperature
Heat Transfer Characteristics
Regime Map of Different Heat Transfer Modes
Conclusions

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