Numerical study of flow boiling in inclined large length-diameter microchannels

The present study aims to numerically investigate the impact of inclination angle on the boiling heat transfer and pressure drop in rectangular microchannel tubes with a large length-diameter ratio. The volume of fluid approach was utilized to model the two-phase flow in microchannels using the computational fluid dynamics method. The effects of different inclination angles, aspect ratio and Reynolds number on heat transfer and pressure drop characteristics are analyzed by simulation. According to the latent heat percentage and saturation temperature differential, the mass transfer factor was calculated using the Lee model, which describes the mass and energy transfer throughout the boiling process. The convective heat transfer coefficients of the walls of structures at angles ranging from 0? to 90? (aspect ratios of 1.271, 1.017 and 0.763, respectively) were analyzed. It was found that with the decrease of aspect ratios, the convective heat transfer coefficients decreased by 16.64% and 11.56%, respectively. In order to keep the evaporator outlet superheat within 5 ?C, the inlet Reynolds number should not be lower than 3000. The study offers insightful information for designing and refining microchannel evaporators in refrigeration systems, particularly for horizontal freezers with specific inclination angle arrangements.