4.6 Article

CFD investigation of R134a and propane condensation in square microchannel using VOF model: Parametric study using steady state solution

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DOI: 10.1016/j.tsep.2023.101662

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Microchannel; Two-phase flow; Condensation; CFD; Volume of fluid

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In this paper, a steady-state analysis is conducted to investigate the condensation of R134a and propane (R290) inside a 0.5-mm square microchannel. A three-dimensional multiphase computational fluid dynamics (CFD) model based on Volume-of-fluid (VOF) approach is developed and validated. The results show different flow regimes transition during condensation and the increase of heat transfer coefficient with increasing mass flux, lower saturation-to-wall temperature difference, and higher inlet vapor quality. Propane is also found to be an environmentally friendly substitute with enhanced heat transfer coefficient compared to R134a.
In this paper, a steady-state analyses of R134a and Propane (R290) condensation inside a 0.5-mm square microchannel are carried out. A three-dimensional (3D) multiphase computational fluid dynamics (CFD) model is developed based on Volume-of fluid (VOF) approach. The model is first validated for mass transfer intensity factor ranging from 60,000 to 400,000 s-1. Thereafter, condensation heat transfer investigation is carried out for different operational conditions including the mass flux ranging from 150 kg/(m(2)center dot s) to 1200 kg/(m(2)center dot s), saturation-to-wall temperature difference ranging from 5 degrees C to 25 degrees C, and inlet vapor quality ranging from 1 to 0.5. The condensation flow regime transition from film annular, wavy annular, plug, slug and fully condensed flow are observed in the obtained simulation results. The average heat transfer coefficient is found to increase with increasing mass flux, low saturation-to-wall temperature difference, and higher inlet vapor quality. In addition, propane is proved to be environmentally friendly substitute of R134a with enhanced heat transfer coefficient by 65-80 % compared to that the latter. The present model allows assessing several two-phase condensing flow parameters with good agreement with literature.

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