Co-current air–water two-phase flow patterns in vertical triangular microchannels

By T. Zhao, Q. Bi. 2001

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Towards uniformly distributed heat, mass and charge: A flow field design study for high pressure and high current density operation of PEM electrolysis cells (2019, methodology): “Figure 4: Flow pattern maps based on data from Zhao and Bi [33].”
Two-phase flow patterns in parallel micro-channels (2003, methodology): “This flow pattern was also observed by Triplett et al. (1999) in the 1.097 mm diameter circular tube and by Zhao and Bi (2001) in the triangular channel of hydraulic diameter of 0.866 mm. This flow, referred by Zhao and Bi (2001) as ‘‘capillary bubbly flow’’, has the following characteristics (as ”
Experimentalstudy on porouscurrentcollectors of PEMelectrolyzers (2012, methodology): “Despite considerable differences in the reported definition of two-phase flow patterns in channels [26-37], it is generally agreed that flow regimes consist of dispersed bubbly flow, slug flow, churn flow, and annular flow.”
The effect of tube diameter on vertical two-phase flow regimes in small tubes (2006, methodology): “diameter, which agrees with Zhao and Bi [ 17 ] and Coleman and Garimella [10] but is”
Effects of Flow Field and Diffusion Layer Properties on Water Accumulation in a PEM Fuel Cell (2007, background): “, [20]), where the water tends to be transported in the corners with the air flowing in the high-velocity core.”