Slug flow, characterized by elongated bubbles flowing in the axial
direction, and gas core flow, which is defined as long gas slug
occupied over a length of channel, were observed. As shown in
Fig. 7a, for the inlet section which led the gas–liquid mixture directly
to the micro-channels, large gas bubbles in the chamber
could expand along the channel length, leading to gas core flow
in most channels.
Slug flow, characterized by elongated bubbles flowing in the axialdirection, and gas core flow, which is defined as long gas slugoccupied over a length of channel, were observed. As shown inFig. 7a, for the inlet section which led the gas–liquid mixture directlyto the micro-channels, large gas bubbles in the chambercould expand along the channel length, leading to gas core flowin most channels.
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