Momentum transfer in an annular duct with upward gas-Iiquid
flow was studied under the condition that the liquid flowed as a film
only on the inner core of the annulus, the outer wall remaining dry.
Previous workers have studied climbing and falling liquid
films in tubes or on vertical planes....
An analysis of the velocity and the shape of large gas bubbles
rising through tubes filled with viscous liquids is presented. Four
tubes, with diameters ranging from 0. 446 inches to 3. 97 inches, and
three liquids, with viscosities ranging from one to 200 centipoise,
were used in the study....
This paper describes a study of two-phase gas-liquid vertical
annular climbing film flow. Using a high speed Fastax movie camera,
motion was slowed sufficiently to facilitate detailed analysis of the
climbing film structure, based on single frame projections. The
dynamic characteristics of the liquid film could likewise be obtained,
though...
The pressure drop for two-phase liquid-liquid flow is theoretically
predicted for each flow regime. Empirical correlations, which
are applicable in all flow regimes, are also presented for holdup as
well as pressure drop.
The experimental study covered bubble and drop flow regimes.
The discontinuous phase was injected by nozzle into...
The momentum transfer characteristics of liquid-liquid dispersions
were studied under conditions of turbulent flow in a cirular
conduit. Experiments were conducted to obtain drop size, friction
factors and velocity profiles for three organic phases dispersed in
water.
The test sections consisted of straight copper tubes 1-inch OD
and 0.830-inch ID....