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tube under churn flow condition.
Since the droplets have great momentum and the length of churn flow is short, the droplets in churn flow show an inevitable effect on the downstream annular flow.
The three flow regimes used were termed bubbly, cap-bubbly, and churn flow.
The vertical flow shows annular flow, churn flow, slug flow, and bubbly flow.
In order to make slug and churn flow artificially, refrigerant-supplying equipment was designed and developed.
This type of flows include cap bubble, slug and churn flow regimes.
These operating regimes have been linked to slug flow and churn flow correspondingly.
These findings provided insight into the distinction between the churn flow and the annular flow.
Understanding the mechanism of droplet entrainment is of great importance for the churn flow.
The literature lacks information on the profile of a huge wave under churn flow condition.
The Sauter diameter of the droplets in churn flow is compared with the existing empirical correlations in annular flow and a formula for the entrained droplet size in churn flow is proposed.
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