Abstract

Flow boiling of water across a bank of circular staggered micro-pin fins, 250 μm long and 100 μm diameter with pitch-to-diameter ratio of 1.5, was experimentally studied for mass fluxes ranging from 346 kg/m 2 s to 794 kg/m 2 s and surface heat fluxes ranging from 20 W/cm 2 to 350 W/cm 2. Local temperature measurements were used to elucidate the two-phase heat transfer coefficients. The flow was visualized and classified as vapor slug and annular flow patterns. A flow map was constructed and compared with maps for adiabatic micro-scale systems and good agreement was observed. A superposition model for the two-phase heat transfer coefficient in convective boiling regime was developed. Frictional multiplier, ( ( ϕ l ) 2 ), from micro-scale studies was used to define the enhancement factor ( F) in the heat transfer coefficient model and reasonable agreement was obtained between experiments and predictions.

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