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Two distinct regimes of homogeneous flow can be identified.
It is close to zero for homogeneous flow patterns like mist and dispersed bubble flows.
Each cell is provided with effective flow fields for a homogeneous flow distribution.
It was observed that the mono-dispersed bubble size distribution stabilized the homogeneous flow regime.
In this section, a homogeneous flow with negligible wall influence is defined as the ideal condition.
Reliable predictions of the homogeneous flow regime with this approach are, however, limited up to now.
Homogeneous flow strongly depends on the structural design of the microchannel reactor.
The two-phase flow model developed was based on the homogeneous flow assumption.
The former produced a poly-dispersed homogeneous flow regime resulting in a concave gas holdup curve, whereas the latter produced a mono-dispersed homogeneous flow regime resulting in an S-shaped gas holdup curve.
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A two-dimensional, pseudo-homogeneous flow model describing such flow patterns is developed.
Analyses are further hampered by short and non-homogeneous flow records.
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