学术文献库

High-fidelity flow boiling simulations are conducted in a vertical minichannel with offset strip fins (OSF) using R113 as a working fluid. Finite-element code PHASTA coupled with level set method for interface capturing is employed to model multiple sequential bubble nucleation using transient three-dimensional approach. The code performance is validated against experiments for a single nucleation site in a vertical rectangular channel. To test the code performance, the studies for a bubble departing from the wall in a minichannel with OSF are carried out first. Due to low heat flux values applied to the channel (1 kW/m2) contribution from the microlayer is not considered. The influence of surface characteristics such as contact angle and liquid superheat on bubble dynamics are analyzed. Local two-phase heat transfer coefficient is also investigated. To achieve higher void fractions, two conic nucleation cavities are introduced in the same channel with OSF. Observed bubble characteristics (departure diameter, bubble departure frequency) are evaluated and bubble trajectories are presented and analyzed. Local heat transfer coefficient is evaluated for each simulation case. The results show approximately 2.5 times increase in the local heat transfer coefficient when individual bubbles approach the wall. With a smaller bubble nucleation diameter, heat transfer coefficient increases by two times. The current work shows the capability of modeling flow boiling phenomena in such complex geometry as OSF as well as data processing advantages of high-resolution simulations.